Pulsed pressure swing adsorption system and method

ABSTRACT

A pressure swing adsorption (PSA) system and methods for controlling each PSA cycle performed by the PSA system to produce oxygen enriched gas during productive portions of a user breathing cycle, and to cease production of oxygen enriched gas during non-productive portions of the user breathing cycle, is provided. The PSA system synchronizes PSA cycle phases including adsorption and desorption phases with a user&#39;s individual inhalation and exhalation phases, on a breath by breath basis, such that each PSA cycle can be dynamically varied from a succeeding PSA cycle, in real time in response to variations in the user&#39;s breathing cycle. An oxygen delivery device including a breathing cycle sensor provides breathing cycle inputs to a controller for use with at least one algorithm to detect breathing flow phases during each user breath, and to synchronize each PSA cycle to the user&#39;s breathing flow phases, on a breath-by-breath basis.

CROSS REFERENCES TO RELATED APPLICATIONS

This application claims priority to and the benefit of U.S. patentapplication Ser. No. 16/704,413 filed Dec. 5, 2019, and U.S. ProvisionalPatent Application 62/775,733 filed Dec. 5, 2018, which are herebyincorporated by reference in their entirety.

TECHNICAL FIELD

The present disclosure relates generally to an oxygen concentrator, andmore particularly to oxygen concentrators including pulsed pressureswing adsorption systems and methods for outputting oxygen enriched gasfrom the oxygen concentrator.

BACKGROUND

Typical atmospheric air consists of two primary types of molecules,nitrogen and oxygen, and lower concentrations of many other substances.Human lungs extract oxygen from atmospheric air via breathing. The humanrespiratory cycle alternates between inhalation, wherein air and henceoxygen is uptake into the lungs, and exhalation, wherein carbon dioxideis expelled from the lungs through a gas exchange process. At rest, thiscycle typically repeats 15-20 times per minute, or every 3 to 4 seconds.During more intense activity, the cycle is repeated more frequently.Humans extract oxygen from the air that flows into the lungs duringinhalation. The vast majority of the oxygen intake is drawn from thevolume of air from roughly the first approximately 70% of theinhalation, however during the final approximately 30% of the inhalationthere is a volume of air in the nose, trachea, and bronchi that althoughinhaled, is exhaled from the human body without gas exchange. This lastvolume of air in each inhalation provides very little to no usefuloxygen to the human body.

Some medical conditions, such as chronic obstructive pulmonary disease(COPD), make human lungs less efficient at extracting oxygen fromatmospheric air. One treatment for these medical conditions is toincrease the fraction of oxygen in the air that the individual breathes.Supplemental oxygen may also be used in other applications, such as inaircraft at high altitude and for athletes recovering from particularlystrenuous activities. Supplemental oxygen may be provided by storingoxygen in a tank which delivers highly concentrated oxygen to cannulasthat connect to the individual's nose. Mobility is improved somewhat byusing a portable oxygen concentrator that produces oxygen from theambient air as opposed to an oxygen storage tank. However, such oxygenconcentrators still impair the individual's mobility due to theirphysical size and weight and limited battery life.

Pressure swing adsorption (PSA) is a cyclical adsorption process whereininlet gas is pressurized and separated to produce a raffinate product.This adsorption process occurs when pressurized inlet gas interacts witha molecular sieve such as zeolite. Air is pressurized, and the nitrogengas component of the inlet air is selectively adsorbed by the molecularsieve compared to the oxygen. This adsorbed gas is then desorbed bydepressurizing the adsorbent bed, therein regenerating the adsorbentbed, allowing for additional product gas such as oxygen to be produced.This product gas production rate depends on several factors such asoxygen recovery and productivity, which are influenced by the cycle timeof the pressure swing adsorption system as well as many other factors.

Portable oxygen concentrators utilize a selectively adsorbent media,such as zeolite. The selective nature means that certain gas components,like nitrogen, are more likely to be adsorbed than other gas components,like oxygen. Furthermore, adsorption varies based on the gas pressure.When air at elevated pressure is passed through a bed containingadsorbent material such as zeolite, the nitrogen in the air is adsorbedinto the zeolite and air with a dramatically higher percentage of oxygenemerging from the zeolite bed. The zeolite's ability to adsorb nitrogenis limited. As the quantity of nitrogen in the zeolite increases, theadsorption rate generally decreases. The zeolite can be “regenerated” bylowering the pressure in the system. At lower pressure, the adsorbednitrogen is desorbed (released) from the zeolite bed. The desorbednitrogen can be vented from the zeolite bed, in some embodiments of theinvention via a different opening. The process of separating oxygen gasfrom nitrogen gas by alternately pressurizing and depressurizing azeolite bed is called Pressure Swing Adsorption (PSA). Since PSAproduces concentrated oxygen only during the adsorption (high pressure)phase, current oxygen concentrators typically utilize multiple zeolitebeds such that at least one adsorbent bed is producing oxygen at alltimes. During one phase, a first bed will be adsorbing while a secondbed is desorbing. During the next phase, the first bed is desorbing, andthe second bed is adsorbing. Each phase typically lasts about 2-4seconds. These devices not only require multiple beds, but also requirea multitude of valves, contributing to their size, weight, powerconsumption, and cost.

Skarstrom cycle pressure swing adsorption systems utilize two adsorbentbeds, a surge tank, and a series of valves to switch between theadsorbent beds. Such pressure swing adsorption systems generatecontinuous output, wherein one adsorbent bed producing raffinate productwhile at the same time the other adsorbent bed is regenerating,switching from adsorption to desorption after a fixed predeterminedperiod of time, also referred to as the cycle time.

SUMMARY

The present disclosure relates generally to systems and methods forpressure swing adsorption systems and oxygen concentrators. Otherembodiments are directed to systems and computer readable mediaassociated with control methods described herein.

An oxygen concentrator system and method for providing oxygen enrichedgas to a user of the oxygen concentrator are described herein. In anillustrative example, the oxygen concentrator includes a pressure swingadsorption (PSA) system including an adsorption column, an aircompressing device configured to output pressurized air, and a gasoutlet configured to flow a first output gas to a user of the oxygenconcentrator. The gas outlet, the air compressing device, and theadsorption column are in fluid communication via a plurality of valves.The PSA system is configured to perform a PSA cycle by selective openingand closing of the plurality of valves, where the PSA cycle includes aplurality of PSA phases including an adsorption phase and a desorptionphase. In one example, the PSA system is configured to produce theoxygen enriched gas during the adsorption phase, and to cease theproduction of the oxygen enriched gas during the desorption phase. Theoxygen concentrator further includes a controller configured to controlexecution of the PSA cycle by selectively actuating the plurality ofvalves to perform the plurality of PSA phases, and to control the flowof the first output gas through the gas outlet, where the first outputgas is the oxygen enriched gas produced by the adsorption column. Theoxygen concentrator includes a sensor in communication with the gasoutlet and the controller, which is configured to sense a breathingparameter of a breathing cycle of the user. The user's breathing cycleincludes a plurality of breaths, with each respective breath of theplurality of breaths including an inhalation phase and an exhalationphase. In one example, the controller is further configured to receive,from the sensor, a breathing input defined by the breathing parameter,and to determine, for each respective breath, using the breathing inputand one or more algorithms, the beginning of the inhalation phase of therespective breath and the beginning of the exhalation phase of therespective breath. The controller is further configured to synchronizeexecution of the PSA cycle with each respective breath such that theadsorption phase is actuated at the beginning of the inhalation phase ofthe respective breath, the desorption phase is actuated at the beginningof the exhalation phase of the respective breath, and the flow of theenriched oxygen gas via the gas outlet is actuated at the beginning ofthe inhalation phase of the respective breath.

The inhalation phase of the user's breath includes a useful period and adead space period, where the dead space period occurs between the usefulperiod and the exhalation phase of the respective breath. In oneexample, the controller is further configured to determine for eachrespective breath, using the breathing input, the beginning of the deadspace period of the inhalation phase, and to synchronize execution ofthe PSA cycle with each respective breath such that the adsorption cycleis ceased at the beginning of the dead space period of the respectivebreath and the flow of oxygen enriched gas via the gas outlet is ceasedat the beginning of the dead space period of the respective breath.

In a non-limiting example, the gas outlet of the oxygen concentratorsystem is configured to flow a second output gas to a user of the oxygenconcentrator, where the second output gas is the pressurized airoutputted from the air compression device and/or a blower included inthe oxygen concentrator system. The controller is further configured tosynchronize execution of each respective PSA cycle with each respectivebreath such that the flow of pressurized air via the gas outlet isactuated at the beginning of the dead space period of the inhalationphase.

In one example, the oxygen concentrator system and/or the controller isconfigured to control the flow of the pressurized air via the outletsuch that the pressured air provides a positive end expiratory pressure(PEEP) to the user. In one example, the controller is configured toactuate the oxygen concentrator to function as one of a continuouspositive airway pressure (CPAP) device and a bilevel airway pressure(BiPAP) device.

In an illustrative example, each respective breath of a user's breathingcycle is immediately preceded in the breathing cycle by a precedingbreath and is immediately succeeded in the breathing cycle by asucceeding breath. Each breath can be described as having an exhalationphase includes a non-useful period and a pre-inhalation period, wherethe pre-inhalation period occurs between the non-useful period of therespective breath and the inhalation phase of the succeeding breath. Inone example, the oxygen concentrator system and/or the controller isfurther configured to determine for each respective breath, using thebreathing input, the beginning of the pre-inhalation period of theexhalation phase, and to synchronize execution of the respective PSAcycle with each respective breath such that the adsorption phase of thePSA cycle for the succeeding breath is actuated at the beginning of thepre-inhalation period of the exhalation phase, the flow of thepressurized air via the gas outlet is ceased at the beginning of thepre-inhalation period of the exhalation phase, and the flow of theenriched oxygen gas via the gas outlet is actuated at the beginning ofthe pre-inhalation period of the exhalation phase.

In one example, the oxygen concentrator system further includes anoxygen delivery device connected to the gas outlet and in communicationwith the controller. The oxygen delivery device can include a cannulaoperatively connected to the gas outlet via the oxygen delivery device,where the user received the output gas from the PSA system via the gasoutlet and the cannula, and a breathing cycle sensor in communicationwith at least one of the cannula and the gas outlet. The cannula can be,for example, a nasal cannula configured to be worn by the user. Thebreathing cycle sensor is configured to sense at least one of abreathing pressure, breathing flowrate, EtCO2, CO2 concentration, and O2concentration of the user, which is outputted to the controller, wherethe controller is further configured to receive, from the breathingcycle sensor, a sensor input, and using the sensor input, determine atleast one of the breathing cycle and an oxygen requirement of the user.

In one example, the PSA system is configured as a pulsed pressure swingadsorption (PPSA) system. In one example, the air compressing deviceincludes at least one microblower. In one example, the oxygenconcentrator system further includes a vacuum device in fluidcommunication with the adsorption column, where the vacuum device isselectively actuable by the controller during the desorption phase toassist in performance of the desorption phase, for example, by flowinggaseous nitrogen desorbed from the adsorption bed out of the adsorptioncolumn and/or PSA system.

The above features and advantages, and other features and advantages, ofthe present disclosure are readily apparent from the following detaileddescription of some of the best modes and other particular embodimentsfor carrying out the invention, as defined in the appended claims, whentaken in connection with the accompanying drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1A shows a phase graph illustrating the flow phases of a humanbreathing cycle including inhalation and exhalation phases;

FIG. 1B (prior art) shows a phase graph illustrating flow phases ofbreathing cycles in conjunction with PSA phases of a PSA cycle of aprior art oxygen concentrator;

FIG. 1C (prior art) shows a phase graph illustrating flow phases ofbreathing cycles in conjunction with PSA phases of a PSA cycle of aprior art oxygen concentrator;

FIG. 1D-E show example phase graphs illustrating flow phases of abreathing cycle in conjunction with PSA phases of a PSA cycle of anoxygen concentrator system of the present invention;

FIG. 1F shows a phase graph illustrating flow phases of breathing cyclesin conjunction with PSA phases of a PSA cycle of an oxygen concentratorsystem of the present invention;

FIG. 1G shows a phase graph illustrating the flow phases of a breathingcycle in conjunction with PSA phases of a PSA cycle of an oxygenconcentrator system of the present invention;

FIG. 1H shows example graphs illustrating breathing flow phases, CO2concentration, and oxygen concentration over time, as related to asynchronization algorithm used for control of the PSA phases of a PSAcycle in some embodiments;

FIG. 1I shows a graph illustrating the user breathing flow phases duringa breathing cycle in conjunction with PSA phases of a PSA cycle of anoxygen concentrator system of the present invention;

FIG. 1J shows a graph illustrating the user breathing flow phases duringa breathing cycle in conjunction with PSA phases of a PSA cycle of anoxygen concentrator system of the present invention;

FIG. 1K shows a graph illustrating the pressure phases of the adsorptioncolumn of a PSA system of the present invention;

FIG. 1L shows a graph illustrating breathing pressure using the flowphases of user breathing cycles in conjunction with oxygen output froman oxygen concentrator in the present invention;

FIG. 1M shows a schematic diagram of an oxygen concentrator breathingcircuit for use with an oxygen delivery device;

FIG. 1N shows a graph illustrating the user breathing flow phases duringuser breathing cycles in conjunction with that of PSA phases of a PSAcycle of an oxygen concentrator in the present invention;

FIG. 2 shows a schematic diagram of a Pressure Swing Adsorption systemaccording to some embodiments;

FIG. 3A shows a schematic diagram of a first example Pressure SwingAdsorption system, including a controller, according to someembodiments;

FIGS. 3B-3E show schematic diagrams illustrating exemplary valve statesand flow directions of air in a breathing cycle as according to theschematic diagram of the first example Pressure Swing Adsorption systemillustrated in FIG. 3A;

FIGS. 3F-3L shows schematic diagrams of additional examples of the firstexample Pressure Swing Adsorption system illustrated in FIG. 3A;

FIG. 4 shows a flowchart describing the PSA phases of a PSA cycle of aPressure Swing Adsorption system corresponding to the inhalation andexhalation cycles of a breathing cycle;

FIG. 5 shows a schematic diagram of a Pressure Swing Adsorption systemaccording to some embodiments;

FIG. 6 shows a schematic diagram of a Pressure Swing Adsorption systemaccording to some embodiments;

FIGS. 7A-B show schematic diagrams of an exemplary Pressure SwingAdsorption system according to some embodiments;

FIG. 8 shows a schematic diagram of an exemplary component of thePressure Swing Adsorption system according to the Pressure SwingAdsorption system of FIGS. 7A-B;

FIGS. 9A-D show schematic diagrams of an exemplary Pressure SwingAdsorption system according to the Pressure Swing Adsorption system ofFIGS. 7A-B;

FIG. 10 shows a schematic diagram of an additional exemplary PressureSwing Adsorption system according to the Pressure Swing Adsorptionsystem of FIGS. 7A-B;

FIG. 11 shows a schematic diagram of an exemplary component of thePressure Swing Adsorption system according to the Pressure SwingAdsorption system of FIG. 10;

FIG. 12 shows a schematic diagram of an exemplary component of thePressure Swing Adsorption system according to the Pressure SwingAdsorption system of FIG. 10;

FIGS. 13A-C shows a schematic diagram of an exemplary Pressure SwingAdsorption system according to some embodiments;

FIG. 14 shows a schematic diagram of an exemplary Pressure SwingAdsorption system according to some embodiments; and

FIG. 15 shows a schematic diagram of an exemplary Vacuum Pressure SwingAdsorption system according to some embodiments.

DETAILED DESCRIPTION

Referring to the drawings, wherein like reference numbers correspond tolike or similar components throughout the several figures, methods andsystems are disclosed herein, relating to pressure swing adsorptionsystems and oxygen concentrators.

I. Exemplary Breathing Cycle and Prior Art Oxygen Concentrators

FIG. 1A shows a phase graph 100 which illustrates an example humanbreathing cycle 102 comprising an inhalation phase and an exhalationphase. Typically, the majority of oxygen intake delivered to a humanbody is drawn from the volume of air inhaled from roughly the first 67%of the inhalation phase. A portion of the air drawn by the human duringthe inhalation phase will not reach the human body. This portion of theair, the last volume, is known as anatomical dead space or dead spaceair, illustrated in FIG. 1A, and provides very little to no usefuloxygen to the human body.

Previous oxygen concentrators are comprised of a two-bed pressure swingadsorption (PSA) system that continuously produces an oxygen enrichedgas output product 110A. The oxygen enriched gas outputted from a PSAsystem can be referred to herein as oxygen output, as oxygen gas, asoxygen concentrated gas, as oxygen product gas, as oxygen, as enrichedoxygen, as oxygen enriched gas, and/or as oxygen enriched product. Asillustrated by the phase graph 100A shown in FIG. 1B (prior art), oxygenoutput 110A is continuously produced during the entire breathing cycle,e.g., during both the inhalation and exhalation phases, of a user of anoxygen concentrator including the PSA system illustrated by phase graph100A, whether or not the user actually demands the oxygen. In thisconfiguration, the continuous output of oxygen 110A will be providedeven if the user is in the exhalation phase of the user's breathingcycle 102A, which is wasteful and unnecessary since oxygen is for themost part only required by the user during the inhalation phase of thebreathing cycle 102A. Further, the adsorption phase 111 of the pressureswing adsorption cycle of the prior art oxygen concentrator illustratedby the phase graph 110A of FIG. 1B is continuous throughout andirrespective of changes in the user breathing cycle 102A. This isbecause with two-bed pressure swing adsorption, one adsorbent bed isalways adsorbing while the other is regenerating. These individualadsorbent beds switch from adsorption to regenerating afterpredetermined fixed periods of time, also referred to as PSA cycletimes. Continuous flow product gas output (oxygen output) 110A is alwaysproduced when the PSA system is operational since there is always oneadsorbent bed that is always in the adsorption phase 111 of the PSAcycle. Thus, neither the oxygen output 110A nor the adsorption phase 111of the prior art continuous flow oxygen concentrator illustrated by FIG.1B is synchronized with the inhalation phase of the user breathing cycle102A.

As illustrated in the phase graph 100B shown in FIG. 1C (prior art),some oxygen concentrators are configured to release an oxygen pulsedosage 110B, to conserve the oxygen product output generated by a PSAsystem of the oxygen concentrator, only releasing the oxygen gas to theuser during the inhalation phase in short 200 to 400 millisecond bursts(pulses) using an oxygen conserving device. This prior art oxygenconserving system includes a pressurized oxygen tank at the outlet ofthe pressure swing adsorption system that primarily delivers oxygen onlyat the initial stage of inhalation, by detecting a drop in pressure assensed by inhalation of a user. This configuration reduces the size ofoxygen concentrators, since more than 67% of continuous flow oxygen isdelivered when the user is not inhaling. However, the prior art pulsedose oxygen output 110B and methods of detection and/or delivery do notmatch a user's oxygen demand as determined by the user's breathing cycle102B, resulting in lower fractions of inspired oxygen (FiO2) as comparedto continuous flow output 110A with equivalent oxygen volumes inspired.Thus, neither the oxygen output 110B nor the adsorption phase 111 of theprior art pulse dose oxygen concentrator illustrated by FIG. 1C issynchronized with the inhalation phase of the user breathing cycle 102B.Further, pulse dose oxygen output 110B and current oxygen concentratorshave several key issues including bulky and energy inefficient oxygenproduction systems, lag times of over 100 milliseconds for oxygendelivery, and fixed volume oxygen output that does not match user demandor adjust breath by breath. The present invention seeks to solve theseproblems in the prior art through on-demand oxygen production using apulsed pressure swing adsorption system as described herein which isconfigured to and/or controlled by methods described herein such thatoxygen enriched gas can be delivered to the user at variable times andat variable and/or in selectable doses automatically determined by theuser's breathing cycle, as illustrated in FIGS. 1D through 15, describedin further detail herein.

There are other drawbacks to pulse dose oxygen output systems such asthe systems illustrated by the phase graphs 110A and 110B of FIGS. 1Band 1C. For example, if the user inhales at a rate faster than the rateat which pressure swing adsorption system continuously produces oxygen,these prior art oxygen concentrators will not output oxygen at all orwill simply output compressor air (non-oxygen enriched) as a fail-safe.This can be harmful to the user in situations where an oxygen user needslarge amounts of oxygen in a short amount of time or breathes at a highnumber of breaths per minute. Some oxygen users must use continuous flowoxygen 110A rather than pulse dose 110B during sleep due to the longershallowing inhalation and exhalation phases of breathing during sleep.In this situation, pulse dose 110B is inadequate compared to continuousflow 110A. Further, for many oxygen users, a setting of “1 LPM” pulsedosage 110B provides less actual oxygenation to the user than 1 LPM ofcontinuous flow oxygen 110A due to the discrepancy between oxygen pulsedosage delivery and actual user oxygen demand. This means that manyoxygen users demand more oxygen than can be provided by pulse dosage. Inprior art pulse dose oxygen concentrators, the oxygen output issynchronized with the inhalation phase of the breathing cycle, howevercontinuous flow oxygen is not output, but rather a short burst or pulseof oxygen 110B.

Further, in previous pulse dose oxygen concentrators, two bed pressureswing adsorptions are used to continuously produce the oxygen and thenpulsed out by an oxygen conservator during a user inhalation. In theseprevious pulse dose oxygen concentrators, the adsorption phase 111 iscontinuous as shown in FIG. 1C, with cycle times of the PSA system beingfixed and irrespective of the user breathing pattern, e.g., the userbreathing cycle 102. Thus, the system is producing oxygen continuously,even though the output of oxygen is only outputted to the user in doses110B. While the oxygen output is synchronized with the inhalation phaseof the user breathing cycle 102B, the PSA adsorption phase 111 is notsynchronized with the inhalation phase of the user breathing cycle 102B.

II. Exemplary Oxygen Output Synchronized with Breathing Cycle

The following invention describes an example of a pressure swingadsorption (PSA) system 10 with one or more adsorbent beds thatcontinuously produces oxygen during the inhalation phase of a user'sbreathing cycle 202, e.g., when the user inhales and which does notproduce oxygen during the exhalation phase of a user's breathing cycle202, e.g., when the user exhales. As used herein, a user's breathingcycle 202 includes a plurality of breaths, each breath includes aninhalation phase and an exhalation phase. In a breathing cycle 202including a plurality of breaths, it would be appreciated that eachbreath can vary from another breath in duration, flow rate, flow volume,flow pressure, etc. Likewise, each inhalation phase can vary induration, pressure, volume, etc. from each other inhalation phase, andeach exhalation phase can vary in duration, pressure, volume, etc. fromeach other exhalation phase. With the disclosed invention, continuousflow oxygen production performance of the pressure swing adsorptionsystem 10 can be optimized such that the PSA system 10 described hereincan be made smaller and be more energy efficient as compared with priorart PSA systems, while enabling controlled changes, e.g., variation, inan amount and timing of oxygen flow output to the user, where the amountand timing of oxygen flow output to the user is determined by, e.g.,defined by and synchronized to the specific user's breathing cycle 202using control methods described herein. As such, the oxygen flow output216 can be varied from breath to breath and within an inhalation phase,where the variable oxygen output can be synchronized to each breath ofthe user's breathing cycle 202. Accordingly, the oxygen concentratorsystem and associated control methods disclosed herein are advantaged bybeing configured to adapt and modify the oxygen output on a breath bybreath basis, to output the oxygen enriched gas to the user during theuseful period of the breathing cycle, and to conserve and/or not produceoxygen enriched gas during the non-useful period of the breathing cycle.Synchronizing oxygen output to the useful period of the breathing cycle,and ceasing oxygen production during the non-useful period of thebreathing cycle, eliminates and/or minimizes the amount of waste oxygenwhich must be generated to ensure minimum oxygen gas requirements aremet for the user of the oxygen concentrator. Waste oxygen, as that termis used herein, refers to oxygen which is outputted by a PSA system 10however is not received by the user, e.g., not exchanged by the userduring respiration. By minimizing and/or eliminating waste oxygenproduction, the amount of oxygen which must be produced by the PSAsystem 10 at any time, e.g., the PSA system capacity, is reduced,allowing for a PSA system of decreased size, weight and content, thusreducing the cost of the system and increasing the convenience andportability of the PSA system to the user.

FIGS. 1D-E illustrate example flow phase graphs 20 of breathing flowphases during user breathing cycles 202 in conjunction with PSA phases211, 221, 231, 241 of PSA cycles of a PSA system 10 included in anoxygen concentrator as described herein, where the oxygen concentratoris configured to provide enriched oxygen product to a user, and wherethe flowrate of the enriched oxygen provided to a user is synchronizedwith the breathing cycle 202 of that specific user. Various embodimentsof a PSA system 10 (see FIG. 1M), such as PSA systems 300, 301, 302,303, 304, 305, 306, 307, 500, 600, 700, 850, 860, 870, 880, 900described herein and illustrated in the figures, are configured toprovide enriched oxygen product to a user at a flowrate which issynchronized to and/or defined by that user's breathing cycle 202, andare provided herein as non-limiting examples. The example PSA systems300, 301, 302, 303, 304, 305, 306, 307, 500, 600, 700, 850, 860, 870,880, 900 may be collectively referred to herein as a PSA system 10,and/or may be referred to as a PSA system 10, for example, whendescribing features of a PSA system 10 which can be incorporated intoone or more of the example PSA systems 300, 301, 302, 303, 304, 305,306, 307, 500, 600, 700, 850, 860, 870, 880, 900. As illustrated by thephase graph 20A shown in FIG. 1D, only a portion of the enriched oxygenprovided during the initial period of the inhalation phase will reach(be received by) the user. This initial period of the inhalation phaseis referred to as the useful period of the inhalation phase, such thateach inhalation phase of a user's breathing cycle is characterized by auseful period followed by a dead space period. When the dead spaceperiod begins toward the end of the inhalation phase, very little oxygenis received by the user. In some examples herein, the useful period ofthe inhalation phase can be referred to as the productive portion of theinhalation phase, and the dead space period can be referred to hereinthe non-production portion of the inhalation phase. In one embodiment,as illustrated by the adsorption phase 211 of the PSA cycle shown inFIG. 1D, the oxygen concentrator can provide enriched oxygen to the userbeginning from the end of the user's exhalation phase, also referred toherein as a pre-inhalation period of the exhalation phase, and/orbeginning at the start of the user's inhalation phase, and can continueto provide enriched oxygen up to the beginning of the dead space periodof the inhalation phase, instead of providing enriched oxygen for thefull inhalation phase, thus avoiding the waste of provide enrichedoxygen during the non-productive dead space period and non-usefulportion of the exhalation phase. In this example shown in FIG. 1D, theperiod during which the oxygen concentrator is providing enriched oxygento the user is the adsorption phase 211, which is actuated by acontroller 380 of the PSA system 10 to begin at the pre-inhalationperiod of the exhalation phase and to continue through the useful periodof the inhalation phase which succeeds the exhalation phase in theuser's breathing cycle 202. In some embodiments, when the dead spaceperiod of the user's inhalation phase is detected or triggered, theoxygen concentrator can switch to an oxygen purge phase 221 in which theoxygen concentrator is continuing to collect and produce enriched oxygenbut is not providing the user with the enriched oxygen being collectedduring the dead space period. At a later point when the user isexhaling, the oxygen concentrator can switch to a desorption phase 241where the release of adsorbed gases collected from the atmospheric airby the adsorption bed of the PSA system 10 can be synchronized with theuser's exhalation phase.

The phase graph 20B shown in FIG. 1E illustrates another example of thePSA phases 211, 221, 231, 241 of the oxygen concentrator in sync withthe user's breathing cycle 202. The PSA phases of the oxygenconcentrator PSA cycle, including an adsorption phase 211, an oxygenpurge phase 221, a pressure equalization phase 231, and a desorptionphase 241 will be discussed in greater detail in the discussion below oflater figures.

In the example phase graph 20C illustrated in FIG. 1F, oxygen enrichedgas 216A can be delivered to the user automatically at variable timesand at variable and/or in selectable doses of the user's breathing cycle202, as defined by user's breathing cycle 202, using a PSA system 10and/or a control method, such as the control method 400 shown in FIG. 4,and as described in further detail herein. In some embodiments, the PSAcycle times and/or the duration of the adsorption phase of the pressureswing adsorption system are variable based on the user's specificbreathing pattern, which can include variability between subsequentinhalation and exhalation breathing phases of the user's breathing cycle202. Hence, with the PSA system and/or oxygen concentrator 10 disclosedherein, the oxygen product gas is produced to the user selectively,e.g., on demand only during the useful oxygen period of the user'sbreathing cycle 202, such as the first 70% of the inhalation phase andnear the end of the exhalation phase, such as the final 10% of theexhalation phase, also referred to herein as the pre-inhalation periodof the exhalation phase. Further, the adsorption phase 211 issynchronized with the useful oxygen period of the user's breathing cycle202, rather than the adsorption phase 211 occurring continuouslythroughout and irrespective of changes in the user breathing cycle 202as seen in prior art (see FIGS. 1B, 1C).

As illustrated in the phase graph 20D shown in FIG. 1G, oxygenconcentrated gas 216B can be delivered to the user automatically atvariable times and at variable doses. In this example, the amount ofoxygen output 216B matches the demand of oxygen from the user. Theoxygen demand is graphically represented by the shaded area under theuser breathing rate curve shown in the phase graph 20D representingvolumetric oxygen output 216B, representing the calculated tidal volumesof the inhalation and exhalations of the user. In this example, thevolumetric oxygen flowrate output is dynamically adjusted using motorand flowrate control in the PSA system 10, synchronized with thechanging oxygen demand of the user. The oxygen output 216B and theadsorption phase 211 of the pressure swing adsorption system 10 are insync with the inhalation and exhalation phases of the user's breathingcycle 202. This could allow for oxygen concentrators that maintain fixedfraction of inspired oxygen (FiO2) ratios for users regardless of theirchanging breathing conditions, improving the clinical efficacy of longterm oxygen therapy for patients with chronic lung diseases such asCOPD.

In the example illustrated in FIG. 1H, in some embodiments of the oxygenconcentrator described herein, one or more sensors are included in theoxygen concentrator for measuring various parameters of the user'sbreathing cycle 202 and/or characteristics of the user's air flow duringthe breathing cycle 202. As shown in an example flowrate graph 204illustrated in FIG. 1H, a user's breathing flowrate values are measuredusing one or more sensors, to compile digital voltage values thatrepresent the flowrate of that user's breathing cycle over time t. Thesebreathing flowrate values are used to determine the different phases ofthat user's breathing cycle, such as the inhalation phase (inhale) andexhalation phase (exhale), as well as determine the time when a user'sbreathing is about to switch from an inhalation phase to an exhalationphase, for example. As illustrated in the flowrate graph 204, duringinhalation the flowrate values are generally negative, while duringexhalation the flowrate values are generally positive. In addition tomeasuring the user's breathing flow 204, and as shown in graph 206,oxygen gas flowrate (O₂ Flow) and/or oxygen concentration (O₂[%]) of theoxygen gas output 216 generated by the PSA system 10 during theadsorption phase 211 of the PSA cycle are also measured. Theconcentrated oxygen gas flowrate and/or oxygen concentration is measuredin order to verify that the PSA adsorption cycle 211 both starts at thecorrect time as well as lasts an appropriate or programmablypredetermined duration, to verify during the control method describedherein, that the PSA adsorption cycle 211 is in sync with the user'sbreathing cycle 202. In one embodiment, a carbon dioxide (CO2)concentration sensor is used to measure and verify the user'sexhalation, as shown in the CO2 concentration (CO₂[%]) graph 208 of FIG.1H. As shown in the CO2 concentration graph 208, the concentration ofcarbon dioxide gas (CO₂[%]) in the gas composition of a user's breathingflow will increase during the exhalation phase, whereas during theuser's inhalation phase, no or only trace amounts of carbon dioxide willbe measured. These different sensor data 204, 206, 208 are measured at ahigh frequency, such as 200 Hz, to dynamically and substantiallycontinuously detect changes in the measured parameters during the user'sbreathing cycle 202. During the measurement period, a synchronizationalgorithm is used to match the user's breathing pattern data with thepulsed PSA oxygen output, to control the PSA system 10 such that theenriched oxygen product 216 is produced and/or outputted to the userprecisely when physiologically most useful. A non-limiting example ofone embodiment of the synchronization algorithm is illustrated by thecontrol method 400 shown in FIG. 4, where oxygen output 216 is providedby an adsorption phase 211 initiated, for example, by a controllerincluded in the PSA system 10 or oxygen concentrator, at a time when theend of the user's exhalation phase and/or the beginning of the user'sinhalation phase is detected and/or determined using one or more, or acombination of, the sensor outputs 204, 206, 208. This synchronizationalgorithm could utilize proportional-integral (PI) control or variousother control algorithms based on measured and/or compiled sensor data.Further, this synchronization algorithm may utilize a circular bufferdata structure to read/write digital sensor values 204, 206, 208 onto aremovable memory device installed to the PSA system 10 and/or the oxygenconcentrator including the PSA system 10, such as an SD card, and/or tostore the digital sensor values 204, 206, 208 to a read only memory(RAM) storage of the microprocessor of the PSA system 10 (see, forexample, microcontroller 814 shown in FIG. 8). Data stored to theremovable memory device, including, for example, digital sensor values204, 206, 208, can be selectively read (collected) from the removablememory device for data processing, for example, by server including oneor more algorithms configured to perform predictive analysis of theuser's breathing, such that the collected data and predictive analysisgenerated using the collected data can be user to improve the accuracyof the synchronization algorithm based on the cumulative collected dataand user's breathing cycle history derived therefrom.

In the example illustrated by the phase graph 20E shown in FIG. 1I,continuous flow oxygen concentrated gas 216A can be delivered by the PSAsystem 10 to the user as determined by the control algorithm 400 and/orusing sensor outputs 204, 206, 208, such that the oxygen output 216A isdelivered to the user automatically at variable selectable times and atvariable and/or selectable doses during inhalation/exhalation period ofthe user's breathing cycle 202. The cycle time of the pressure swingadsorption system, including the time that the PSA cycle is in theadsorption phase 211 and the time that the PSA cycle is in thedesorption phase 241, is variable from one inhalation/exhalation periodof the user's breathing cycle 202 to the next inhalation/exhalationperiod of the user's breathing cycle 202, and determined based on theuser breathing pattern and the control algorithm of the PSA system 10.Hence, with the present invention, the oxygen product gas 216A isproduced during only the useful periods of the breathing cycle, such asthe first 70% of the inhalation phase, also referred to herein as theuseful period of the inhalation phase, and the end of the exhalationphase, also referred to herein as the pre-inhalation period of theexhalation phase. In some embodiments of the PSA system 10, when oxygengas 216A is not being produced by the PSA system 10, such as during adesorption phase 241 activated during most of the exhalation phase of auser's breathing cycle, pressurized air 236 is outputted from the PSAsystem 10 and/or the oxygen concentrator, to the user. In one example,the pressurized air 236 is outputted during a pressurized air phase 231which corresponds in time with the desorption phase 241. Thispressurized air output 236 helps keep the user's airways open duringexhalation by providing a positive end expiratory pressure (PEEP) andcould be psychologically useful in improving user comfort with theiroxygen concentrator or by allowing the oxygen concentrator to functionas an integrated CPAP or BiPAP device, or mechanical ventilator. Thispressurized air 236 can also be used to flush out dead space in a CPAPmask or other masks for breathing therein.

In another example illustrated by the phase graph 20F shown in FIG. 1J,an algorithm is illustrated which controls the delivery of oxygenconcentrated gas 216 to the user of an oxygen concentrator at variableselectable times and at variable and/or selectable doses, where in thepresent example, alternating volumes of oxygen concentrated gas 216 andpressurized air 236 are delivered to the user during the productiveportion of the breathing cycle 202, beginning at a pre-inhalation periodat the end of the exhalation phase and/or beginning at the onset of theinhalation phase, and continuing to the beginning of the dead spaceperiod of the inhalation phase. A non-productive portion of thebreathing cycle 202 can be described herein as including the dead spaceperiod of the inhalation phase and the non-useful period of theexhalation phase.

The cycle times of the alternating adsorption (A) phases 211 and thedesorption (D) phases 241 executed by the PSA system during theproductive portion of the breathing cycle 202 are variable based on theuser breathing pattern 202, however the PSA cycle time, of each pair ofadsorption and desorption phases 211, 241 defining a PSA cycle, is muchfaster than standard inhalation and exhalation time periods. Hence, withthe present invention, the oxygen product gas 216 is producedintermittently during the inhalation phase due to the rapid PSA cycletime and the multiple PSA cycles which are executed during theinhalation phase, as shown in FIG. 1J. In the example shown, the PSAcycle time can be determined as the time elapsed from the start of oneadsorption phase 211 to the start of the subsequent (next) adsorptionphase 211, which includes the duration of the desorption phase 241occurring between the adsorption phases 211. During the desorption (D)phase 241 of each of these rapid PSA cycles, pressurized air 236 can beoutputted in order to maintain positive pressure to the user, and toallow at least some useful gas exchange while oxygen concentrated gas216 is not being produced. This rapid PSA cycle can operate such thatminiature pulses of oxygen concentrated gas 216 and pressurized air 236are intermittently produced only during the useful period of thebreathing cycle 202, where the useful period in the illustrative exampleincludes the first 70% of the duration of an inhalation phase and theend period of the exhalation phase preceding the inhalation phase. Inone example, approximately the last 10% of the preceding exhalationphase is included in the useful period. In the present example, duringthe non-useful periods of the breathing cycle, where the non-usefulperiods can include most of the exhalation phase of a user's breathingcycle and/or the anatomical dead space period of a user's inhalationphase, pressurized air 236 can be output to the user and a longerduration PSA desorption phase can occur, as shown in FIG. 1J. Thislonger duration output of pressurized air 236 during the non-usefulperiod including most of the exhalation phase helps to keep airways openduring exhalation by providing a positive end expiratory pressure (PEEP)to the user, which can be an advantage of the PSA system describedherein, where the PEEP provided by the longer duration of pressurizedair 236 output during the non-useful period(s) is psychologically usefulin improving user comfort with their oxygen concentrator and/or byallowing the oxygen concentrator to function as an integrated CPAP orBiPAP device. Alternatively, with a rapid PSA system 10, two adsorbentbeds can be alternately cycled with rapid PSA cycle times to produceminiature pulses of oxygen, creating a continuous flow of oxygen ondemand when physiologically useful. As used herein, the term “miniaturepulses of oxygen” in intended to mean that more than one oxygen pulse isoutput per period of respiration, e.g., each of the more than one pulsesof oxygen gas outputted per breath consisting of an inhalation phase andan adjacent (either preceding or succeeding) exhalation phase isconsidered a miniature pulse. In this configuration, when oxygen is notbeing produced, the oxygen generator ceases operation, savingapproximately 70% on energy. In some embodiments, the oxygenconcentrator operating in the rapid cycle PSA mode shown in FIG. 1J,could store some non-outputted oxygen volume in a reserve tank, forrelease to the user during higher peak oxygen demand periods occurringduring the breathing cycle 202. In instances of non-spontaneous userbreathing, the oxygen output 216 can be set at a certain breathingfrequency, for example 12 breaths per minute, and the pressurized air236 can be used to provide a PEEP during exhalation, allowing the oxygenconcentrator to provide ventilatory support and/or function as amechanical ventilator where no oxygen-air blending is required, butrather where both the PEEP air pressure 236 from an air blower andoxygen output 236 from the oxygen source such as an oxygen concentratoras described herein are produced and dynamically adjusted on demand forthe user.

As illustrated in FIG. 1K, viewed in conjunction with the examplebreathing cycle shown in FIG. 1L, the steps of the pressure swingadsorption system 10 are synchronized with different pressure phases ofa user breathing cycle 202. Some of these PSA steps could has a fixedduration, e.g., be performed in a fixed amount of time, whereas othersteps may have a variable duration, e.g., be performed in an amount oftime which may vary from one breath to another in the breathing cycle.In the example illustrated by FIG. 1K, in graph 258, the air pressure252 in an adsorbent column 220, 320 of the PSA system 10 is shown, inconjunction with the air pressure 256 in an inlet air volume tank of thePSA system 10 shown in graph 254, where the variation in the pressures252, 256 is shown over time and during steps of the PSA system 10. Forexample, in one embodiment the pressurization step of the PSA cycle isthe fixed amount of time required to pressurize the adsorbent columnwith X cubic inches of air at X liter per minute (LPM) flowrate. In someembodiments, the inlet air volume tank is accumulating pressurized airduring the blowback and O2 purge stages of the PSA cycle, at an inletair volume tank pressure 256. Hence, during the pulsed PSA cycle in thisexample, the pressurization step would occur at the same time as theblowback and O2 purge steps as shown in FIG. 1K. In some embodiments,the pressurization and feed steps of the PSA cycle are the same (STEP1). In one embodiment, the feed step would be a variable amount of timefor adsorption/oxygen production. This feed step would be synchronizedwith user breathing such that in some embodiments the feed step beginsnear the end of the exhalation phase, e.g., after approximately 90% ofthe exhalation phase is completed (0.9E) during the pre-inhalationperiod of the exhalation phase, and terminates at 70-80% of theinhalation phase (0.71), e.g., at the beginning of the anatomical deadspace period (0.71). In one embodiment, the O2 purge fill step (STEP 2)is a variable amount of time based on O2 production during feed as wellas the purge to feed volume desired. The purge to feed ratio isgenerally a fixed ratio, and affects the purity of the raffinateproduct, in this case oxygen. In some instances, this purge to feedratio is determined based on flowrates and not on volumes. In apreferred embodiment, the O2 purge tank is sized so that the tank volumeis filled or nearly filled at a certain purge to feed ratio at most(typical) user breathing rates. In one embodiment, blowback (STEP 3)occurs over a fixed amount of time based on the time required todepressurize the adsorbent column of X volume. In another embodiment,the purge step (STEP 4) is a variable amount of time based on when theend time of the exhalation phase is nearing and/or when oxygenproduction starts (see graph 264). In one embodiment, the blowback andpurge steps are a fixed ratio of one another. In another embodiment, theblowback and purge steps may be combined as one step. Referring to thebreathing cycle 202 shown in FIG. 1L, during rise in rate of breathingpressure (during exhalation) 262, after a certain threshold value ofbreathing pressure 262 is met, STEP 2 starts (see FIGS. 1K and 1L). Whenslope of breathing pressure rise starts falling (see FIGS. 1K and 1L),STEP 3 starts and lasts until after local maxima value reached. Whenbreathing pressure 262 starts falling or flatlines, both in value andrate of change, Step 4 starts (see FIGS. 1K and 1L. Step 4 terminatesnear end of the exhalation phase, then STEP 1 starts for the subsequentinhale/exhale phases of the user's next breath flow. STEP 1 continuesthrough the fall in breathing pressure (inhalation) 262 and then endswhen a certain pressure threshold is reached as determined by rise inthe breathing pressure value 262 and rate of change. These thresholdvalues and rates of change could be experimentally determined orcomputed based on mathematical formulas or different control schema,such as multi-predictive control. To make the prediction of timing ofinhalation versus exhalation phases more accurate, as well asdetermining when to switch PSA steps, a plurality of sensors could beused to correlate data, for example, as described related to FIG. 1H.These different types of sensors can include mass air flow sensors, O2concentration sensors, and CO2 concentration sensors. Capnography withCO2 concentration sensor could be used to determine, e.g., diagnosislung obstructions and/or user oxygen saturation on a breath by breathbasis, allowing for the automatic adjustment of oxygen flowrate andvolume output from PSA system 10 to the user on a breath by breathbasis. This data allows for dynamic air compressor output feedbackcontrol, which would allow the oxygen output 216 from the oxygenconcentrator to be adjusted at a very fast rate, for example, in a rapidPSA cycle configuration. In some embodiments, fraction of inspiredoxygen (FiO2) sensors can also be used to measure the amount of oxygeninspired per breath and to output a volume/flowrate of oxygen per breaththat keeps the FiO2 level constant in accordance with recognizedclinical standards. In other embodiments, a pulse oximeter can beconnected to the oxygen concentrator device via a connector or remotelyconnected to the oxygen concentrator via a near field communicationmethod such as Bluetooth in order to provide the oxygen concentratorcontrol system with blood oxygen saturation, SpO2 or PaO2, data. Thiscould allow for the on demand production of oxygen wherein the oxygenflowrate and/or oxygen gas volume produced is dynamically adjusted viafeedback control or other control algorithm on a breath by breath basisto dynamically maintain constant blood oxygen saturations withinrecognized clinical standards, without users being required to manuallyand/or continually adjust the flowrate of their oxygen concentrator.Dynamic adjustment of the oxygen flowrate and/or volume outputted to theuser on a breath by breath basis present the advantage of improving theclinical efficacy of long term oxygen therapy during situations such assleep or exercise where users have a limited ability to manually adjusttheir oxygen flowrate settings on their oxygen concentrator machine.

In other embodiments, the oxygen output from the oxygen concentrator canbe dynamically adjusted during exercise based on other sensormeasurements such as the volume of oxygen consumed per minute (VO2),which can be measured using an oxygen concentration sensor andcalculated by taking the volume of oxygen inspired per minute andsubtracting it from the volume of oxygen expired per minute. This VO2value over time can be used to determine whether the body is oxygendeficient in the beginning of exercise, for example when the rate of VO2is increasing. This means that the volume of oxygen naturally inspiredwas unable to meet the human body's biochemical ATP (Adenosine5′-triphosphate) demands at the beginning of exercise. The volume of CO2produced per minute (VCO2) can be measured using a CO2 concentrationsensor and calculated by finding the volume of CO2 expired per minuteand subtracting the volume of CO2 inspired per minute. These VO2 andVCO2 values can be used to calculate respiratory exchange ratio (RER),which can be used to determine cardiovascular performance and changingenvironmental conditions related to user exercise and fat oxidation thatare important in athletics. Supplemental oxygen could be useful toathletes or even those with chronic lung diseases in situations wherethere is an oxygen deficit at the beginning of exercise as well asexcess post-oxygen consumption after the exercise has ended. The presentdisclosure details a method of identifying these changes in userbreathing conditions during exercise using sensor(s) and compensatingwith additional supplemental oxygen in a manner that is most beneficialfor the user and efficient for the oxygen production system, whilewasting as little oxygen as possible.

As illustrated in FIG. 1L, a pressure versus time graph 262 of a userbreathing cycle 202 is shown. In this illustration, STEP 1 is a combinedpressurization and feed step wherein oxygen output 216 is produced. Thisoxygen output time tx in STEP 1 corresponds to certain times/portion(s)of the breathing pressure curve 262 therein. STEP 2 represents the O2purge fill phase of the PSA cycle, and corresponds to certaintimes/portion(s) of the breathing pressure curve 262 therein. STEP 3represents the blowback step in the PSA cycle, and corresponds tocertain times/portion(s) of the breathing pressure data therein. STEP 4represents the O2 purge phase 221 in the PSA cycle, and corresponds tocertain times/portion(s) of the breathing pressure curve therein. Asshown in FIG. 1L, the PSA cycle repeats, beginning again with STEP 1,where oxygen output 216 is produced for an oxygen output time tx+1. Inone example, oxygen concentrator and/or PSA system 10 is configured suchthat the oxygen output times tx and tx+1 are equal and constant for eachinhalation/exhalation phase pair of the breathing cycle 202. In someembodiments, the oxygen concentrator and/or PSA system 10 is configuredsuch that the oxygen output times tx and tx+1 are determined by theuser's breathing cycle 202 using sensor inputs from one or morebreathing cycle sensors 16, 18 (see FIG. 1M), which may includebreathing pressure input 262 received from the pressure sensor 16,and/or an algorithm for determining the duration of the oxygen outputtime for each inhalation/exhalation phase pair, where the duration ofoxygen output time may be variable from each inhalation/exhalation phasepair to the next, for example, during a period of erratic user breathingas shown by the variation in breathing pressure 262 in FIG. 1L, suchthat tx and tx+1 may have different durations. In some embodiments, theonset of the oxygen output times tx, tx+1 may be determined based on theuser's breathing cycle 202 using sensor inputs from one or morebreathing cycle sensors 16, 18 (see FIG. 1M), which may includebreathing pressure 262, and/or an algorithm for determining the time toinitiate oxygen output 216 (onset time) for each inhalation/exhalationphase pair, where the onset time for each cycle of oxygen output 216 maybe variable from each inhalation/exhalation phase pair to the next.

Referring to FIG. 1M, a non-limiting example of an oxygen concentratoris shown, including a breathing circuit 30 a PSA system 10 in fluidcommunication with a cannula 12, such that the PSA system 10 canselectively provide an outputted gas to the cannula 12, where theoutputted gas can be an oxygen enriched gas 216 and/or pressurized air236. The oxygen concentrator and/or breathing circuit 30 includes one ormore breathing cycle sensors 16, 18 which are in fluid communicationwith the cannula 12, and configured to sense and/or measure data valuesand rates of change thereof to allow the determination of various phasesof a user's breathing cycle 202, such as exhalation and inhalation, by acontroller in communication with the breathing cycle sensors 16, 18,when the oxygen concentrator is in use by the user. In one example, thebreathing circuit 30 optionally includes an air blower 14 which can beactuated to output pressurized air 236 to the cannula 12, for output tothe user. The controller can be a controller 380 of the PSA system 10,which may be in communication with one or more of the air blower 14, thebreathing pressure sensor 16, and/or the breathing cycle sensors 18. Inone example, the breathing pressure sensor 16, the breathing cyclesensors 18, and/or the air blower 14 can be arranged to define an oxygendelivery device 342. The oxygen delivery device 342 can be incommunication with the controller 380 of the PSA system 10, wherein inthis example, the controller 380 can receive data from the sensors 16,18 and can include one or more algorithm which can be used fordetermining and/or estimating the breathing cycle 202 of the user,and/or generating instructions and/or commands to the PSA system 10and/or the air blower 14 for the selective operation of these elements.In one example, the controller 380 can be included in the oxygendelivery device 342 and/or otherwise included in the oxygen concentratorsuch that the controller 380 is in communication with the breathingcircuit 30 to receive data therefrom and to generate instructions and/orcommands for the operation thereof.

In the example shown, the PSA system 10, the air blower 14, thebreathing pressure sensor 16, and the breathing cycle sensors 18 areeach in fluid communication with a nasal cannula 12, wherein the nasalcannula 12 is wearable by the user to deliver the oxygen enriched gas216 and/or pressurized air 236 from the PSA system 10 and/or air blower14 to the user's respiratory system, for example, via the user's nasalpassages. These sensor data measurements could include, but are notlimited to: EtCO2, CO2 concentration, O2 concentration, breathingflowrates, breathing pressures, etc. In this diagram, any PSA system 10,including but not limited to the exemplary PSA systems 200, 300, 301,302, 303, 304, 305, 306, 307, 500, 600, 700, 850, 860, 870, 880, 900,could be used wherein the oxygen output 216 can be continuous orintermittent. Other types of oxygen generators/storage devices could besubstituted for the PSA system 10 shown in FIG. 1M, in some embodimentsof this disclosure. These other types of oxygen generators/storagedevices include cryogenic distillation, gaseous oxygen tanks, liquidoxygen tanks, membrane oxygen generators, thermal swing adsorptionoxygen generators, chemical based oxygen generators, and hybrid systemsthereof integrated with or separate from the PSA system 10. An airblower 14 can also be integrated to generate positive end expiratorypressure (PEEP) during the exhalation phases of a user's breathing cycle202. Further, check valve(s) and wye tubing could be incorporated intothe breathing circuit 30, to separate the sensors 16, 18 and outputoxygen/air, allowing for more reliable data readings from the sensor(s)16, 18 during both inhalation and/or exhalation phases of the user'sbreathing cycle 202. In some of the embodiments disclosed herein, thesensor outputs from sensors 16, 18 can be received by a controller, suchas a controller 380, 580, 680, 814, and inputted to and/or utilized byone or more algorithms which may be stored to or accessed by thecontroller, to determine one or more of an oxygen output 216 durationtime, onset time, etc. and/or to control operation of the PSA system 10and/or other components of the oxygen concentrator including, forexample, an air blower 14, etc. In a non-limiting example, one or moreof the pressure sensor 16, air blower 14, user breathing cycle sensors18, and/or nasal cannula 12 can be included in an oxygen delivery device342 used in conjunction with a PSA system 10, as described furtherherein.

As illustrated by the phase graph 20G shown in FIG. 1N, oxygen can beoutput from an oxygen volume and/or flowrate can be dynamically adjustedduring the physiologically useful phases of respiration during a user'sbreathing cycle 202. In one embodiment disclosed herein, a pressureswing adsorption system 10 with rapid PSA cycle times can output one ormore pulses of oxygen of varying volumes/flowrates during a singleuseful phase of respiration, as illustrated by the oxygen outputsequences 216C, 216D shown in FIG. 1N. In the example shown, each of thefirst and second oxygen output sequences 216C, 216D is comprised ofalternating oxygen pulses outputted from first and second adsorbent bedsof a PSA system 10. This oxygen volume and/or flowrate output can bedynamically adjusted per pulse or discrete time period (i.e. 50milliseconds) using proportional valve control, DC motor control, airvolume tanks, and/or a combination thereof. Further, during thenon-useful phases of the breathing cycle 202, such as during theexhalation phase, the pressure swing adsorption system 10 may be turnedOFF in order to reduce energy consumption, allowing for oxygen output tobe conserved. In another embodiment, a volume of oxygen may be producedand/or accumulated and stored using an air volume tank, for example,during the non-productive portion of the breathing cycle 202 (the deadspace period of the inhalation cycle and the non-useful period of theexhalation cycle), and then released during a productive portion of thebreathing cycle 202, for example, during the useful period of theinhalation phase and/or during the pre-inhalation period of theexhalation phase. In some embodiments, particularly with rapid PSA cycletimes, a pressure swing adsorption system 10 with two or more adsorbentcolumns, each including an absorbent bed, can be utilized such that eachadsorbent column can have, for example, different physicalcharacteristics such as size and oxygen output production capabilities.This could allow for more variation in oxygen concentrator flow outputand could allow for the production of complex oxygen flow waveforms thatare similar to, e.g., substantially duplicative of, actual user breaths,where the complex oxygen flow waveforms can be created by the controller380 using algorithms and/or controls strategies including but notlimited to: varying cycle times between the adsorbent columns per oxygenpulse, adjusting the oxygen pulse durations, controlling the input aircompressor pressure, flowrates, duty cycle, and/or power consumption,storing oxygen output and/or air input in volume tanks, valve controlsuch as proportional valve control that allows for the regulation and/orconstriction of gas flowrates and/or pressures, as well as creation ofgas output or input waveforms that affect oxygen production or deliveryperformance and/or physical characteristics. Further, these oxygenoutput volumes and/or flowrates may be controlled such that the oxygenoutput volumes and/or flowrates can be varied on a breath by breathbasis, as well as on a pulse by pulse basis. The oxygen concentrator caninclude a controller and/or one or more algorithms that can embody apredictive control schema, which can be used, for example, inconjunction with data collected from sensors 16, 18, to measure a user'sbreathing flowrates and then integrate to calculate a tidal volume. Insome embodiments, a fraction of inspired oxygen (FiO2) percentage, canbe set or programmed into the machine in order to clinically saturate anoxygen patient (user) without requiring adjustment of oxygen settings bythe user. Miniature oxygen pulses can be output for brief periods oftime each, for example 10 milliseconds, such that an oxygen deliverydevice (see 342 at FIG. 3G) which may include one or more sensors 16,18, in conjunction with a controller 380, can estimate the amount ofoxygen that should be delivered in each oxygen pulse based on rate ofchange measured in user breathing flow patterns, in order to maintainthe FiO2 percentage. In one example, after this O2 pulse is delivered,the control system 380, for example, via an algorithm, verifies theaccuracy of the prediction, e.g., the estimate, by integrating thedetected user's breathing flowrate during the time period of that oxygenpulse to calculate a tidal volume, as well as to calculate the oxygenvolume produced/output during this time period. An actual FiO2percentage during this brief time period such as 10 milliseconds iscalculated, and then, via the controller 380 and/or the oxygen deliverydevice 342, compensated for in the next oxygen pulse using feedforwardcontrol, to bring the FiO2 to the set/programmed percentage. In someembodiments, other metrics for the breathing cycle 202, user respirationand cardiovascular health such as VCO2, VO2, SpO2, SpCO2, and/or PaO2can be measured by the oxygen concentrator and used to adjust the oxygenvolume and/or flowrate from the oxygen concentrator to the user, on abreath by breath basis, as required to maintain clinical oxygenation forthe patient, e.g., the oxygen volume and/or flowrate can be adjusted bythe controller 3080 and/or oxygen delivery device 342 if the FiO2percentage maintained is not sufficient for clinical oxygenation for thepatient. Further, these other respiration and cardiovascular healthmetrics can also be used to automatically adjust the FiO2 percentage,via the controller 380 and/or the oxygen concentrator on a breath bybreath, or even intra-breath interval, based on factors estimated suchas lung obstructions, level of activity, blood oxygen saturations,effectiveness of lung gas exchange, and/or anticipated future oxygendemand.

In some embodiments, one or more algorithms can embody a predictivecontrol schema, which can be used, for example, in conjunction with datacollected from the sensors 16, 18, to measure a user's breathingflowrate through one or more breaths, and then manipulate and/orotherwise analyze the collected data to predict and/or estimate theduration of each breathing cycle phase and/or period within a breathingphase, such that the prediction and/or estimation determined therefromcan be used to control initiation and cessation of outputted gas flow atcertain times within the flow phases of succeeding breaths of the user.In one example, the control system 380, for example, via an algorithmand data collected during the succeeding breaths of the user, verifiesthe accuracy of the prediction and/or estimate, and uses the differencesbetween the predicted and/or estimated value and the actual value toincrease the accuracy of the prediction and/or estimation algorithmsover time. In this example, the algorithms are configured as learningalgorithms which are adapted over time and as actual user data isaccumulated, to increase the accuracy of the algorithms to predict theindividual user's breathing cycle 202 such that the timing, flow rate,volume, etc., of outputted oxygen gas 216 and/or pressurized air 236 canbe customized with high accuracy to each breath of the user, on a breathby breath basis.

III. Exemplary Oxygen Concentrator

An exemplary oxygen concentrator including a PSA system 10, for example,a PSA system 300, 301, 302, 303, 304, 305, 306, 307, 500, 600, 700, 850,860, 870, 880, 900 as described in multiple embodiments, is providedherein and illustrated by the accompanying figures. In one example, anoxygen concentrator is provided with a single adsorption bed that usesthe pressure swing adsorption process to provide oxygen enriched gas toa user. In this example, the pressure swing adsorption system uses acyclical adsorption process where inlet gas, from atmospheric gases, ispressurized and separated to produce a raffinate product. Specifically,the inlet gas can be atmospheric air and the product produced by thepressure swing adsorption is an enriched oxygen product such that theoxygen concentration of the product gas exceeds that of normalatmospheric air, which is 21%.

Referring now to FIG. 2, shown is a first example of a pulsed pressureswing adsorption system. In this example, a pressure swing adsorption(PSA) system 200 comprises a compressor 210, an adsorption column 220,and an oxygen purge tank 230. The compressor 210, adsorption column 220,and oxygen purge tank 230 can be connected to each other in series. Aplurality of valves such as valve 240, valve 250, valve 260, and valve270 operably connect each of the compressor 210, adsorption column 220,and oxygen purge tank 230 and act as gates for either allowing orblocking gas to flow through each of the valves 240, 250, 260, 270.

During an adsorption phase 211 of the PSA system 200, the compressor 210compresses atmospheric air, also referred to herein as feed air,pressurizes the atmospheric air, and delivers the pressurized air 236 tothe adsorption column 220. The atmospheric air is substantiallycomprised of oxygen and nitrogen gas. Once the pressurized air 236 isdelivered to the adsorption column 220, the adsorption column 220 willadsorb the nitrogen gas from the pressurized air 236, such that theremaining pressurized air 236 becomes oxygen enriched, e.g., iscomprised of a greater percentage of oxygen as compared to theatmospheric air. As shown in FIG. 2, the oxygen enriched gas 216, alsoreferred to herein as oxygen gas, comprising the remaining pressurizedair 236 continues to flow through an open valve 250 to the oxygen purgetank 230. The oxygen gas will continue to flow through the oxygen purgetank 230 and to a user who inhales the oxygen gas 216 generated by,e.g., outputted from, the PSA system 200.

In one example, the adsorption column 220 contains an adsorption bed,such as adsorption bed 755 shown in FIG. 7, comprising molecular sievessuch as zeolite or Lithium Type-X zeolite (Li—X zeolite). During theadsorption phase 211, the zeolite will adsorb the atmospheric nitrogenfrom the pressurized air, allowing oxygen to pass through the adsorptioncolumn 220 and into the oxygen purge tank 230.

At a desorption phase 241 of the PSA cycle of the PSA system 200, valve250 is closed and blocks oxygen from flowing between the adsorptioncolumn 220 and the oxygen purge tank 230. During the desorption phase241, valve 270 is open allowing the adsorption column 220 to desorb,such that pressurized nitrogen gas stored in the adsorption column 220during the adsorption phase 211 is depressurized from the adsorption bedand exits the PSA system 200 via the open valve 270, back into theatmosphere, therein regenerating the adsorbent bed. Once the nitrogen isreleased from the adsorption column 220 through the open valve 270, asubsequent adsorption phase 211 is initiated, whereby via the process ofadsorption enriched oxygen can be provided to a user, as previouslydescribed. The PSA system 200 repeats the alternating desorption andadsorption phases 241, 211 in a PSA cycle, to generate and provideoxygen gas to a user of the oxygen concentrator including the PSA system200.

IV. Pulsed PSA System

FIGS. 3A-I illustrate examples of a pressure swing adsorption system. Inthis example, referring to FIG. 3A, a pressure swing adsorption system300 is described. The pressure swing adsorption system 300 generatesraffinate product such as enriched oxygen in a non-continuous manner, inoxygen pulses 216. In one example, the PSA system 300 is apulsed-pressure swing adsorption system. The PSA system 300 minimizesoxygen output waste by only providing oxygen gas to a user during theportion of the user's breathing cycle 202 where the oxygen gas isphysiologically useful to the user. In some embodiments, the PSA system300 will not release oxygen to the user during the user's exhalationphase, or during the later period of the inhalation phase correspondingto the anatomical dead space period.

In this example, illustrated in FIG. 3A, the PSA system 300 comprises acompressor 310, an adsorption column 320, and an oxygen purge tank 330.The compressor 310, adsorption column 320, and oxygen purge tank 330 canbe connected to each other in series as shown in FIG. 2. A plurality ofvalves such as valve 340, valve 350, valve 360, and valve 370 operablyconnects each of the compressor 310, adsorption column 320, and oxygenpurge tank 330 and acts as gates for either allowing or blocking gas toflow through each of the valves 340, 350, 360 and 370. The PSA system300 can also include a controller 380 which can monitor and control theamount and direction of flow of the gases by controlling the valves 340,350, 360, and 370. In one example, the valves 340, 350, and 370 aretwo-way solenoid valves and valve 360 is a 3-way solenoid valve. Thememory of the controller 380 can include, by way of example, sufficientread only memory (ROM), Random Access Memory (RAM),electrically-erasable programmable read only memory (EEPROM), etc.,i.e., non-transient/tangible machine memory optical memory, flash orother solid state memory, and the like of a size and speed sufficient tostore data received, for example, from sensors 16, 18, and/or an oxygendelivery device 342, and to store one or more algorithms and/or controlstrategies for selectively actuating the PSA system 300 including one ormore of a plurality of valves, to generate oxygen gas, to manipulatedata received by the controller, and/or to execute the algorithms and/orcontrol strategies stored thereon. Transitory memory such as randomaccess memory (RAM) and electrically-erasable programmable read-onlymemory (EEPROM) may also be included, along with other requiredcircuitry (not shown), including but not limited to a high-speed clock,current/voltage/temperature/speed/position sensing circuitry,analog-to-digital (A/D) circuitry, digital-to-analog (D/A) circuitry, adigital signal processor, and any necessary input/output (I/O) devicesand other signal conditioning and/or buffer circuitry, as required toexecute the methods and processes described herein.

In the present example, valve 360 is a three-position or three-wayvalve. In one position, valve 360 connects an outlet of compressor 310output to an inlet of adsorption column 320 while blocking flow to anair release to the atmosphere. In a second position, valve 360 connectsthe outlet of the compressor 310 to the air release while blocking flowto the adsorption column 320. Valve 370 can be a normally-closed two-waysolenoid valve which selectively connects the inlet of adsorption column320 (or, alternatively, a separate port) to the nitrogen release. Valve350 can be a normally-closed two-way solenoid valve which selectivelyconnects an outlet of adsorption column 320 to an inlet of an oxygenpurge tank 330. An outlet of adsorption column 320 is connected to aninlet of oxygen purge tank 330 through valve 350. Oxygen purge tank 330provides a volume for storage of concentrated and/or enriched oxygen gas216. Valve 340 can be a normally-closed two-way solenoid valve whichselectively connects an outlet of the oxygen purge tank 330 to a releasesuch that a user can breathe in the oxygen gas 216 from the oxygen purgetank 330. In one example, controller 380 can control and change thestate of valves 340, 350, 360, and 370 to switch the system among theseveral PSA phases 211, 221, 231, 241, described in detail below. Thecontroller 380 synchronizes execution of the PSA phases 211, 221, 231,241 performed by the PSA system 300 with the user's breathing cycle 202such that oxygen gas 216 is selectively output during the useful portionof each inhalation phase and such that oxygen gas 216 is not output whennot physiologically useful to the user, in accordance with one or morecontrol algorithms executed by the controller 380.

FIGS. 3B-3E show the flow and direction of gases at the different PSAphases 211, 221, 231, 241 of the PSA system 300 occurring during aninhalation phase and subsequent exhalation phase of a user's breathingcycle 202. As illustrated in FIG. 1E, the PSA phases of a PSA cycle ofoperation of the PSA system 300 are an adsorption phase 211, oxygenpurge phase 221, pressure equalization phase 231, and desorption phase241. As illustrated in FIG. 1E, the phases of the PSA cycle aresynchronized with the inhalation and exhalation phases of the user'sbreathing cycle 202. In the example shown and referring to FIG. 1E, theadsorption phase 211 is synchronized, e.g., in sync, with the portion ofthe inhalation phase not including the anatomical dead space period. Theoxygen purge phase 221 is in sync with the anatomical dead space period.The pressure equalization phase 231 is in sync with a first portion ofthe user's exhalation period. And the desorption phase 241 is in syncwith a second portion of the user's exhalation period.

In an illustrative example, the adsorption phase 211, synced with auser's inhalation period, has a duration of about or approximately 1.5seconds. The oxygen purge phase 221, synced with a user's anatomicaldead space period and the pressure equalization phase 231, synced withthe first portion of the user's exhalation period, each have a durationof about or approximately 0.5 seconds. The desorption phase 241, syncedwith the second portion of the user's exhalation period, has a durationof about or approximately 2.5 seconds. The example breathing cycle 202and the PSA cycle times provided herein are merely illustrative of thatof an average user of the oxygen concentrator, and as such arenon-limiting. Breathing rates and inhalation to exhalation time ratiosare unique to each user. As further described herein, the oxygenconcentrator of the present disclosure can include a control system,executed for example, by a controller 380, 580, designed to detect thelength of each inhalation and exhalation phase of an individual user,and utilize data generated from that particular individual user'sinhalation and exhalation phases, to control the adsorption anddesorption phases 211, 241 of the pulsed PSA process in sync with thebreathing cycle 202 of that particular individual user over time, e.g.,over a plurality of inhalation and exhalation phases.

A. 4-Phase Pulsed PSA Cycle

The following describes the four phases 211, 221, 231, 241 of the PSAcycle performed by the example PSA system 300 illustrated in FIG. 3A.Each of the four phases 211, 221, 231, 241 is respectively illustratedin each of the FIGS. 3B, 3C, 3D, 3E. The PSA cycle or process executedby the phases 211, 221, 231, 241 illustrated in FIGS. 3A-3E is referredto herein as a 4-Phase Pulsed PSA Cycle. The oxygen concentratorincluding the PSA system 300 can include a controller 380 and an oxygendelivery device 342 in communication with the controller 380, asillustrated for example, in FIGS. 3G and 3H, where in FIGS. 3A-3E thecontroller 380 and the oxygen delivery device 342 have been removed forillustrative purposes only. In one example, the PSA system 302 includesan air filter 312 connected to the compressor 310 to filter outparticles other than atmospheric air from the atmosphere to thecompressor 310.

The example described herein is non-limiting, as PSA systems can howeverhave a different number of steps or phases depending on theconfiguration.

1. Adsorption

Referring to FIGS. 1E and 3B, FIG. 3B shows the device of FIG. 3A in theadsorption phase 211. The controller 380 can enter the adsorption phase211 either at the beginning of the inhalation phase, slightly before, orslightly after the beginning of inhalation phase of the user's breathingcycle 202, depending on the control schema and/or algorithm used tocontrol operation of the oxygen concentrator including the PSA system300. During the adsorption phase 211, valve 360 is set to connect theoutput of compressor 310 to the inlet of adsorption column 320. Valve370 is closed. At this point, the compressor receives atmospheric airand pressurizes the atmospheric air to create pressurized air 236 andoutputs the pressurized air 236 through the valve 360 to the inlet ofadsorption column 320. As this pressurized air 236 flows and diffusesthrough the adsorption column 320, the nitrogen in the pressurized air236 is adsorbed, and the oxygen product gas 216 is released at theoutlet. In one example, the pressurized air 236 is greater than 1atmospheric pressure. The adsorption column 320 contains zeolite whichadsorbs the nitrogen from the pressurized air 236.

At this point, valve 370 is closed in an “off” position. Valve 350 isopen in an “on” position. The oxygen enriched gas 216, absent most ofthe nitrogen, flows from the adsorption column 320, through valve 350,to the oxygen purge tank 330, resulting in a pressure drop across theadsorption column 320. Pressure in oxygen purge tank 330 is onlyslightly higher than atmospheric pressure during this phase. Valve 340is also set to open such that concentrated oxygen gas 216 flows from theoxygen purge tank 330 to the user.

2. Oxygen Purge

Referring to FIGS. 1E and 3C, FIG. 3C shows the device of FIG. 3A in theoxygen purge phase 221. The controller 380 actuates the PSA system 300to enter this phase at during the dead zone of the inhalation phase, asdetected by input received from sensors 16, 18 and/or as determined byone or more algorithms execute by the controller 380. Valve 360 remainsset to connect the output of compressor 310 to the inlet of adsorptioncolumn 320. Valve 370 remains closed and valve 350 remains open. Valve340 is now switched to closed in an “off” position, preventing flow ofenriched oxygen 216 from the oxygen purge tank 330 to the user. Asconcentrated oxygen flows from adsorption column 320 into oxygen purgetank 330, pressure in oxygen purge tank 330 increases, although itremains less than the pressure of atmospheric air entering adsorptioncolumn 320.

3. Pressure Equalization

Referring to FIGS. 1E and 3D, FIG. 3D shows the device of FIG. 3A in thepressure equalization phase 231. Valve 360 is set to direct thepressurized air from 236 compressor 310 to an air release, such that nomore pressurized atmospheric air is being supplied into the adsorptioncolumn 320. The inlet of adsorption column 320 is blocked by both valve360 and valve 370. Valve 350 is closed blocking flow between adsorptioncolumn 320 and oxygen purge tank 330. During this phase, the pressuredifferential across adsorption column 320 dissipates such that the airpressure over the entire adsorption bed in the adsorption column 320settles at an intermediate value. In the pressure equalization phase231, adsorption is minimal and/or ceases, such that neither oxygenenriched gas 216 is produced from the pressurized atmospheric air 236nor is enriched oxygen 216 outputted from the PSA system 300 to theuser.

4. Desorption (Nitrogen Release)

Referring to FIGS. 1E and 3E, FIG. 3E shows the device of FIG. 3A in thedesorption phase 241. The controller 380 actuates the PSA system 300 toenters this desorption phase 341 during the exhalation phase of theuser's breathing cycle 202, at a time determined by the controller 380based on data received from sensors 16, 18 and/or as determined by thecontroller 380 and/or one or more algorithms executed by the controller380. Valve 340 remains closed. Valve 360 remains in the same position asthe pressure equalization phase. Valves 350 and 370 are opened in an“on” position allowing flow. Valve 340 remains closed in an “off”position since during exhalation, the user does not need oxygen. Duringthis phase, the pressure gradient through adsorption column 320reverses, such that the outlet is at higher pressure than at the inletof the adsorption column 320. As the pressure in adsorption column 320decreases, nitrogen is desorbed from the adsorption bed, e.g., nitrogenre-enters the gaseous state in the adsorption column 320. The pressuregradient causes the gaseous nitrogen to flow out the inlet of theadsorption column 320, through valve 370, such that the desorbed gaseousnitrogen is released via valve 370 back into the atmosphere. A portionof the concentrated oxygen 216 flows from oxygen purge tank 330 backinto adsorption column 320 to balance the nitrogen gas exiting via thevalve 370. When the controller 380 senses that the exhalation phase isalmost over, it actuates the PSA system 300 return to the adsorptionphase 211 of FIG. 3B and the PSA cycle repeats.

B. PPSA with 3-Way Valve and Nitrogen Release Combined

Another example configuration of a PSA system 300 is illustrated by thepulsed PSA (PPSA) system 301 shown in FIG. 3F. The oxygen concentratorincluding the PSA system 301 can include a controller 380 and an oxygendelivery device 342 in communication with the controller 380, asillustrated for example, in FIGS. 3G and 3H, where in FIG. 3F thecontroller 380 and the oxygen delivery device 342 have been removed forillustrative purposes only. In this example, a compressor 310 draws inatmospheric air and compresses it, in one example, to a pressure ofabout 2-4 atmospheres. In some embodiments this pressure output could belower than 2 atmospheres or higher than 4 atmospheres. The temperaturecan also increase due to adiabatic compression. In some examples, thecompressor 310 can include some storage volume and/or a heat exchanger.In one example, the air can be cooled after leaving the compressor 310in order to increase the adiabatic efficiency of the adsorption phase211. In another example, this pressure swing adsorption process can bethermally assisted wherein during the adsorption phase 211 theadsorption column 320 is cooled during the adsorption phase 211 andheated during the desorption phase 241. In another example, the oxygenpurge gas 216 in the oxygen purge tank 330 can be heated in order toincrease the adiabatic efficiency of the desorption phase 241. In theexample shown in FIG. 3F, valve 372 can be a three-way solenoid valve.In one configuration, for example, the “ON” configuration, valve 372connects the output from the compressor 310 to an inlet of adsorptioncolumn 320 while blocking flow to the nitrogen release. In anotherconfiguration, valve 372 connects the inlet of the adsorption column 320to the nitrogen release while blocking flow from the compressor 310. Anoutlet of the adsorption column 320 is connected to an inlet of theoxygen purge tank 330. The adsorption column 320 contains a selectivelyadsorbent material, such as zeolite, as previously described herein. Theoxygen purge tank 330 provides a volume for storage of concentratedoxygen gas 216. The controller 380 changes the state of valves 372, 340,and 350 to switch the system among the several phases of the PSA cycleas described herein. In one example, the controller 380 is incommunication with and receives at least one input from an oxygendelivery device 342 that measures the breathing pattern characteristicsof a user using an oxygen concentrator including the PSA system 301, toactuate the PSA system 301 in response to phases of the user's breathingcycle 202 detected by and/or estimated by the controller 380 using theinput received from the oxygen delivery device 342. In one example, theoxygen delivery device 342 includes one or more sensors 16, 18 (see FIG.1M) to sense parameters such as flowrate and/or air pressure of theuser's breathing, and to output data to the controller 380 related tothese parameters. The oxygen delivery device 342 may include sensor orother measurement devices such as mass air flow sensor(s), pressuretransducer(s), oxygen concentration sensor(s), and/or carbon dioxideconcentration sensor(s), which may provide data to the controller 380for use in conjunction with one or more algorithms to determine and/orestimate the exhalation and inhalation phases of the user's breathingcycle 202. The controller 380 synchronizes the PSA phases 211, 241 ofoperation of the PSA system 301 with the user's breathing cycle 202 suchthat oxygen enriched gas 216 is produced by and/or outputted from thePSA system 301 during the useful portion of each inhalation phase andduring the pre-inhalation period of each exhalation phase of theindividual user's breathing cycle 202. In one example, the controller380 synchronization between the different sensor or data outputs couldbe performed using a synchronization algorithm, comprising one or morecontrol methods such as time-based control, pressure-based control,and/or gas composition-based control. In one example, delivery of theoxygen gas 216 is initiated near the end of each user exhalation phase,e.g., during a pre-inhalation period of the exhalation phase, to allowoxygen pooling at the beginning of each user inhalation phase, improvinguser oxygenation.

In one example, the compressor 310 in the PSA system 302 does not haveto receive and compress air constantly. The compressor 310 can bevariably controlled by the controller 380 such that the compressor 310can be in an “ON” or “OFF” state where only the adsorption and oxygenpurge phases 211, 221 will allow the compressor 310 to deliverpressurized air 236 to the adsorption column 320. This way, instead ofthe compressor 310 always providing pressurized air 236 and having avalve to direct air into or away from the adsorption column 320depending on the phase of the PSA system 300, the compressor 310 canprovide air by turning on or off. In one example, the controller 380includes a pulse width modulation (PWM) control that controls the powerof the compressor 310. In another example, the controller 380 caninclude at least one MOSFET switch (see 812 in FIG. 8) to regulate thepower of the compressor 310 by turning it on or off. Powering thecompressor 310 on and off also dissipates heat more effectively from thePSA system 301. In one example, an air pressure tank 332 (see FIG. 3H,for example) can be combined with a pressure switch in order to turn offthe compressor once the pressure inside the air pressure tank 332reaches a certain pressure value. In one example, a brushless DCelectric motor is used to power the air compressor 310, wherein higherintermittent loading allows for a more compact PSA system 10 as comparedto continuously loaded/operated motors used in prior art PSA systems.Further, DC motor control can be used to regulate and dynamically adjustair compressor flowrate and pressure, allowing for changes in oxygenoutput 216 from the PSA system 10 on a breath by breath basis, e.g.,adjustments to the oxygen output 216 can be made for everyexhalation/inhalation phase pair of the user's breathing cycle 202 suchthat the oxygen concentrator dynamically responds to changes and/orirregularities in the individual user's breathing pattern. This DC motorcontrol could also be used in conjunction with proportional valvecontrol and a surge tank, wherein oxygen accumulates in the surge tankand is produced by a pulsed PSA system 10 that utilizes one or moreadsorbent columns 320, wherein the PSA cycle times of the pulsed PSAsystem 10 in the present invention are not the same as user breathingand/or could be constant values.

During operation of the PSA system 301 shown in FIG. 3F, at theadsorption phase 211, similar to that of the adsorption phase 211 of thePSA system 300 shown in FIG. 3B, the controller 380 of the PSA system301 actuates the beginning of the adsorption phase 211 at the beginningof the user's inhalation phase or slightly before the beginning of theuser's inhalation phase, e.g., toward the end of the user's exhalationphase. During the adsorption phase 211, valve 372 is set to connect theoutput of compressor 310 to the inlet of adsorption column 320. As thecompressed air flows into the adsorption column 320, nitrogen in thecompressed air is adsorbed into the zeolite of the adsorption bed,increasing the relative oxygen content of the compressed air in theadsorbent column 320. The air, absent most of the nitrogen, flows fromthe adsorption column 320 to oxygen purge tank 330 through valve 350 atan “on” configuration, with a resultant pressure drop across theadsorption column 320. In one example, the pressure drop is lower thanthe pressure provided from the compressor 310 and hence oxygen enrichedproduct 216 flows out from the adsorbent column 320. Pressure in theoxygen purge tank 330 is only slightly higher than atmospheric pressureduring this phase. Valve 340 is at an “on” configuration such thatconcentrated oxygen 216 flows from oxygen purge tank 330 to the user.

At the oxygen purge phase 221, similar to that of the oxygen purge phase221 of FIG. 3C, the controller 380 of FIG. 3F initiates actuation of theoxygen purge phase 221 at the during the dead zone of the inhalationphase of the user's breathing phase 221. Valve 372 remains set toconnect the output of compressor 310 to the inlet of adsorption column320. Valve 340 is closed, preventing the flow of oxygen gas from theoxygen purge tank 330 to the user. As concentrated oxygen flows fromadsorption column 320 into oxygen purge tank 330, pressure in oxygenpurge tank 330 increases, although it remains less than the pressure ofair entering adsorption column 320.

During operation of the desorption phase 241 of the PSA system 301,similar to that of desorption phase 241 of PSA system 300, thecontroller 380 of PSA system 301 actuates the PSA system 301 to enterthe desorption phase 241 during the user's exhalation phase as detectedand/or determined by the controller 380. During the desorption phase241, the valve 340 remains closed. Valve 372 is switched to connect theinlet of adsorption column 320 to a nitrogen release. During thedesorption phase 241, the pressure gradient through the adsorptioncolumn 320 reverses such that the pressure at the outlet is at higherpressure than at the pressure at the inlet. As the pressure inadsorption column 320 decreases, nitrogen desorbs from the adsorptionbed, e.g., is released in a gaseous form from the adsorption bed andinto the adsorption column 320. The pressure gradient causes thenitrogen to flow out the inlet of the adsorption column 320, throughvalve 372, to the nitrogen release. During release of the nitrogen gas,some concentrated oxygen flows from oxygen purge tank 330 back intoadsorption column 320. When the controller 380 senses that the user'sexhalation phase is almost over, it returns operation of the PSA system301 to the adsorption phase 211 and the PSA cycle repeats.

C. PPSA with Oxygen Delivery Device with Pressure Sensor

In another example configuration of the PSA system 300, a pulsed PSA(PPSA) system 302 is shown in FIG. 3G and includes an oxygen deliverydevice 342 in communication with the controller 380. The oxygen deliverydevice 342 is connected to the oxygen purge tank 330 through the valve340 such that the oxygen delivery device 342 is the physical interfacethat delivers the enriched oxygen 216 from the oxygen purge tank 330 tothe user. In one example, the oxygen delivery device 342 comprises acannula and/or airline 12 (see FIG. 1M) that can engage the user fordelivery of the oxygen enriched gas 216 to the user's respiratorysystem, for example, via the nasal passages of the user. In one example,the oxygen delivery device 342 comprises at least one pressure sensor 16(see FIG. 1M) that can sense and detect the beginning of each inhalationphase and the beginning of each exhalation phase of the breathing cycle202 of a user of an oxygen concentrator including the PSA system 302 andoxygen delivery device 342. In some examples, the oxygen delivery device342 can include one or more user breathing cycle sensors 18, asdescribed related to FIG. 1M, which can be in communication with thecontroller 380, such that the controller 380 receives data from thepressure and breathing cycle sensors 16, 18 and can utilize the receiveddata to dynamically determine and/or estimate the exhalation andinhalation phases of the user's breathing cycle 202 in real time, and todynamically synchronize the PSA valve actuation sequences that controlthe adsorption, oxygen purge, pressure equalization, and desorptionphases 211, 221, 231, 241 of the PSA cycle with that the breathing cycle202 of the user in real time. In one example, the oxygen delivery device342 measures flowrate or air pressure of the user's breathing, forexample, using sensors 18. The controller 380 synchronizes actuationand/or duration of each of the 211, 221, 231, 241 phases of the PSAsystem 302 with the user's breathing such that oxygen enriched gas 216is produced and/or outputted to the user during the physiologicallyuseful portions of respiration, e.g., during the useful period of theuser's inhalation phase prior to the anatomical dead space period, andduring the pre-inhalation period of the user's exhalation phase.

In one example, the controller 380 can be configured to include adefault setting for the oxygen flow cycle. The default setting can beset, for example, at 15 breaths per minute when the PSA system 10 isinitially turned on, e.g., powered up by a user of the oxygenconcentrator. The controller 380 can be configured to actuate the PSAsystem 10 to start the adsorption phase 211 only when the breathingpressure sensor 16 reaches a defined threshold indicating a point intime within an inhalation phase and/or exhalation phase of the breathingcycle 202 of the user. In one example, the pressure threshold can bebased on a negative threshold pressure, such as −0.06 centimeter ofwater (cmH2O). The controller 380, for subsequent breaths, e.g., forinhalation and exhalation phases succeeding the user's initial breaths,can use the data collection from the breathing pressure sensor 16 duringthe initial breaths to change the oxygen flow cycle of the oxygenconcentrator for each succeeding breath, which can include changing oneor more of the oxygen production volume, the oxygen flowrate, and thetime at which oxygen output 216 is initiated for each succeedingbreathing phase, depending on the breathing pattern of the user sensedby pressure sensor 16. Alternatively, the controller 380 can alsoconfigure the PSA system 300 to not deliver oxygen when the breathingpressure sensor 16 detects and/or the controller 380 determines that theuser is not breathing in air or there are other failed triggers that donot justify outputting the enriched oxygen gas 216 from the PSA system300. The default setting for a particular user can also change based onthe user's specific breathing pattern using control algorithms includingbut not limited to one or a combination of multi-predictive, PI, PID,feedback, and/or feedforward controls which may be stored in andexecuted by the controller 380.

In one embodiment, the compressor 310 can be operated intermittently inorder to reduce energy consumption when not utilized during theadsorption phase for a pulsed pressure swing adsorption system 303. Inone embodiment, this is accomplished using a MOSFET switch 812 to turnthe air compressor 310 ON or OFF. In a different embodiment, wherein thecompressor 310 utilizes an electric motor, pulsed width modulation (PWM)control could be utilized and synchronized with the adsorption, oxygenpurge, and desorption steps of the pulsed PSA cycle. In one embodiment,a pressure switch can be used in conjunction with an air pressure tank332 to turn off the compressor. Further, when operated intermittently(for example, 1 second ON, 3 seconds OFF, etc.) as compared tocontinuously, the air compressor or diaphragm pump can more effectivelydissipate heat from the PSA system 10. This increases thermodynamicefficiency and allows the electric motor to utilize higher voltages orloading when powered on, without causing overheating. In this example,higher air flowrates and pressure outputs can be obtained from arelatively smaller compressor 310, with the advantage of a decreasedpackaging space requirements for the smaller compressor 310, and anassociated decrease in the size of the PSA system 10.

D. PPSA with 2^(nd) Air Pressure Tank after Compressor

In an alternate example of the PSA system 300, a PSA system 303 is shownin FIG. 3H which includes the addition of an air pressure tank 332. ThePSA system 303 can include a controller, such as the controller 380illustrated in FIGS. 3A-G, where the controller 380 is not shown in FIG.3H for illustrative purposes only. In this example, pressurized air 236that is not used during the desorption phase 241 can be stored andutilized when the pulsed PSA system 303 switches to the adsorption phase211 and/or to the oxygen purge phase 221. This configuration iscontrasted with that of PSA system 300 of FIG. 3A. In this example, atwo-way valve 390 is provided instead of the three-way valve 360included in PSA system 300, which releases the pressurized air 236 backinto the atmosphere. In the example shown in FIG. 3H, the air pressuretank 332 can be utilized as an energy storage device, where pressurizedair 236 is stored for periods of higher than normal oxygen demand andreleased to the adsorption column 320 to produce larger volumes ofoxygen enriched gas 216 during the higher demand inhalation phases.Alternatively, the air pressure tank 332 can be utilized as an energystorage device at specific times during the inhalation phase, such asduring the useful period, e.g., the productive portion, of theinhalation phase. In one example, the PSA system 303 can include anadditional valve (not shown) in which waste air from a continuous flowair compressor can be output.

E. PPSA without 2-Way Valve Between Oxygen Purge Tank and AdsorptionColumn

In an alternate example of the PSA system 300, a PSA system 304 isillustrated in FIG. 3I and described herein. The oxygen concentratorincluding the PSA system 304 can include one or more breathing cyclesensors 16, 18 and/or an oxygen delivery device 342 in communicationwith the controller 380, as illustrated for example, in FIGS. 3G and 3H,where in FIG. 3I the oxygen delivery device 342 has been removed forillustrative purposes only. Similar to the PSA system 300 shown in FIG.3A, the PSA system 304 of FIG. 3I does not include a two-way valvebetween the adsorption column 320 and oxygen purge tank 330. The PSAsystem 304 comprises a compressor 310, an adsorption column 320, and anoxygen purge tank 330. The compressor 310, adsorption column 320, andoxygen purge tank 330 can be connected to each other in series, as shownin FIG. 3I. A plurality of valves such as valve 340, valve 360, andvalve 370 operably connect each of the compressor 310, the adsorptioncolumn 320, and the oxygen purge tank 330 and act as gates for eitherallowing or blocking gas to flow through each of the valves, where thevalves 340, 360, 370 can be selectively actuated by the controller 380to operate the PSA system 304 in the various PSA phases, as described indetail herein. The controller 380 is configured to monitor and controlthe amount, direction, and timing of the flow of the gases into and outfrom the PSA system 304 by controlling the valves 340, 360, and 370. Inone example, the valves 340, and 370 are two-way solenoid valves andvalve 360 is a 3-way solenoid valve. The three-way valve 360, whenactuated in a first position, e.g., in a first valve state, connects theoutput of the compressor 310 to an inlet of the adsorption column 320while blocking flow to an air release which when open, e.g., unblocked,vents to the atmosphere. In a second position, e.g., in a second valvestate, the valve 360 connects the outlet of the compressor to the airrelease while blocking flow to the adsorption column 320. Valve 370 canbe a normally-closed two-way solenoid valve which selectively connectsthe inlet of the adsorption column 320 (or, alternatively, a separateport) to the nitrogen release. Oxygen purge tank 330 provides a volumefor storage of concentrated and/or enriched oxygen gas 216. Valve 340can be a normally-closed two-way solenoid valve which selectivelyconnects an outlet of the oxygen purge tank 330 to a release such that auser can breathe in the oxygen enriched gas 216 from the oxygen purgetank 330 when the valve 340 is released, e.g., in an open position. Inone example, the controller 380 can control and change the state ofvalves 340, 360, and 370 to switch the system among the several PSAphases, as described herein. The controller 380 uses one or morealgorithms to synchronize each PSA phase of operation of the PSA system304 with the each breathing phase of the user's breathing cycle, e.g.,with each breath taken by the user, to control the operation of the PSAsystem 304 such that oxygen enriched gas 216 is outputted during theproductive portion of the inhalation phase and/or during the productiveportion of the exhalation phase of each user breath, and such that theoutput of oxygen enriched gas 216 is minimized or ceased during thenon-productive portions of the user's breathing cycle 202, such asduring the anatomical dead space period of the inhalation phase andduring the non-useful period of the exhalation phase of each breath ofthe user's breathing cycle 202. The productive portion of the user'sinhalation phase can also be referred to herein as the useful period ofthe inhalation phase. The exhalation phase of the user's breathing cycle202 can be characterized as including a non-useful period followed by apre-inhalation period, where in an illustrative example shown in FIG. 1Fthe pre-inhalation period occurs between the non-useful period and asucceeding inhalation phase of the user's breathing cycle 202.

In this example, the PSA System 304 of FIG. 3I differs from that of PSAsystem 300 such that the PSA system 304 does not include a two-way valve(see valve 350 in PSA system 300) between the adsorption column 320 andoxygen purge tank 330. Effectively, the steps of the PSA system 304 aresimilar to that of the 4-Phase Pulsed PSA cycle but instead do notinclude the pressure equalization phase 231. The functions of thepressure equalization phase 231 are, in the example PSA system 304 shownin FIG. 3I, combined with that of the oxygen purge phase 221. In oneexample, the PSA cycle of the PSA system 304 is consistent with that ofFIG. 1G. Effectively, the configuration of the Pulsed PSA system 304 canbe applied to that of any of the other PSA systems 10.

F. Vacuum PPSA

FIGS. 3J, 3K, and 3L illustrate an alternate examples of a single bedoxygen concentrator, including, respectively, a vacuum pulsed PSA (PPSA)system 305, 306, 307. The PSA systems 305, 306, 307 each include acontroller 380, as illustrated for example, in FIGS. 3A-G, where inFIGS. 3J, 3K, and 3L the controller 380 has been removed forillustrative purposes only. The oxygen concentrators including the PSAsystems 305, 306, 307 can each include one or more breathing cyclesensors 16, 18 and/or an oxygen delivery device 342 in communicationwith the controller 380, as illustrated for example, in FIGS. 3G and 3H,where in FIGS. 3J, 3K, and 3L the oxygen delivery device 342 has beenremoved for illustrative purposes only. As illustrated in FIG. 3J, asingle bed oxygen concentrator is shown including a PSA system 305 whichincludes both a compressor 310 and a vacuum compressor 312. In theexample shown, valve 372 is a three-way solenoid valve. In one valvestate of the valve 372, the valve configuration, for example, the “ON”state, the valve 372 connects the outlet of the compressor 310 to aninlet of the adsorption column 320 while blocking flow to the nitrogenrelease, e.g., where the nitrogen release can occur via the outlet fromthe compressor 310 when the state of the valve 372 is changed. Inanother configuration, valve 372 connects the inlet of adsorption column320 to the nitrogen release while blocking flow of pressurizedatmospheric air, for example, from the vacuum compressor 312 and thecompressor 310, into the adsorption column 320. In one example, othercomponents, including at least one cooling fan, can be included in thePSA system 10, including the present example PSA system 305, to coolcomponents of the PSA system 10.

One advantage of the Vacuum Pressure Swing Adsorption (VPSA) systemshown in FIGS. 3J, 3K, and 3L, is the fact that VPSA allows for a longeradsorbent column lifecycle and higher adsorbent productivity sinceadsorbed products are more easily removed using vacuum depressurizationas compare with removal of adsorbed products using an oxygen gas purgephase 221. Further, VPSA, in some examples, yields oxygen enriched gas216 which is characterized by a higher O2 purity than oxygen enrichedgas 216 produced from a non-VPSA system 10.

At the adsorption phase 211, similar to that of adsorption phase 211 ofthe PSA system 300 shown in FIG. 3B, the controller 380 actuates theVPSA system 305 to initiate the adsorption phase 211 at the beginning ofthe inhalation phase or at a pre-inhalation period of the exhalationphase occurring slightly before the beginning of the inhalation phase.During the adsorption phase 211, valve 372 of the VPSA system 305connects the output of the compressor 310 to the inlet of adsorptioncolumn 320, such that pressurized air 236 flows from the compressor 310over the adsorption bed of the adsorption column 320, where nitrogen inthe compressed air 236 is adsorbed into the zeolite, and the oxygenenriched air 216, absent most of the nitrogen, flows from the adsorptioncolumn 320 to oxygen purge tank 330, with a resultant pressure dropoccurring across the adsorption column 320. The air pressure at theoutlet of adsorption column 320 is only slightly higher than atmosphericpressure during this adsorption phase 211. During the adsorption phase211, valve 340 is set to open such that the concentrated oxygen gas 216flows to, e.g., is outputted to, the user, for example, via a cannula 12(not shown) connected to the output of the valve 340 and VPSA system305.

When operating in a desorption phase 241, similar to that of desorptionphase 241 of FIG. 3E, the controller 380 actuates the VPSA system 305 toenter the desorption phase 241 during the beginning of the exhalationphase of the user's breathing cycle. During the desorption phase, eachof the valves 340 and 350 are in the “OFF” configuration, or closedstate, and valve 372 is in an open state to connect the inlet ofadsorption column 320 to the inlet of the vacuum compressor 312. Thevacuum compressor 312 is actuated such that, during the desorption phase241, the pressure gradient through adsorption column 320 reverses suchthat the air pressure at the outlet of the adsorption column 320 is athigher pressure than the air pressure at the inlet of the adsorptioncolumn 320. Due to the sub-atmospheric pressures created by theoperation of the vacuum pump 312, an oxygen purge stage 221 is notneeded to remove the adsorbed nitrogen from the adsorbent column 320.Rather, as the pressure in adsorption column 320 decreases, nitrogendesorbs from the adsorbent bed into a gaseous state in the adsorptioncolumn 320 and the desorbed nitrogen gas is released via an exhaustoutlet 317 of the vacuum compressor 312 back into the atmosphere. Thepressure gradient created by the vacuum compressor 312 causes thenitrogen gas to flow out the inlet of the adsorption column 320, throughvalve 372 and vacuum compressor 312, to the nitrogen release outlet. Insome embodiments, the controller 380 actuates valve 350 to an openedstate, to release a volume or flowrate of concentrated oxygen from theoxygen purge tank 330, which flows back into desorbed adsorption column320. When the controller 380 determines, for example, using datareceived from one or more sensors 14, 16, that the exhalation phase ofthe user is almost over, e.g., is approaching a pre-inhalation period inthe exhalation phase, the controller 380 actuates the VPSA system 305 toreturn to the adsorption phase 211, and repeats the PSA cycle.

FIG. 3K illustrates another example PSA system 306 which utilizes avacuum during the desorption phase 241, such that the PSA system 306 canbe described as a VPSA system 306. In the example shown in FIG. 3K, theVPSA system 306 includes a combined vacuum pump and compressor 314, alsoreferred to herein as a dual compressor 314, instead of a separatecompressor 310 and vacuum compressor 312. By using a dual compressor314, less packaging space is required within the oxygen concentrator,such that this configuration is advantaged by a more compact designwhich may be more convenient and portable for a user. In the exampleshown, valve 373 connects the dual compressor 314 and the adsorptioncolumn 320. In one example, the valve 373 is configured as a two-wayvalve, where in a first valve state, for example, an “ON” configuration,valve 373 connects an outlet of the dual compressor 314 output to aninlet of adsorption column 320 while blocking flow to a nitrogen releaseoutlet. The dual compressor 314 is selectively actuable by thecontroller 380 to operate in one of a compressor mode and a vacuum mode,where in the compressor mode the dual compressor 314 operates to inputpressurized air 236 from the atmosphere into the adsorption column 320,and in a vacuum mode operates to extract gas from the inlet of theadsorption column 320 and to pump the extracted gas toward the nitrogenoutlet, creating a volume of air having substantially lower pressurethan the atmospheric pressure of the air at the inlet. During operationof the VPSA system 306, the controller 380, in response to data inputsreceived from an oxygen delivery device 342 and/or sensors 16, 18measuring flowrate or air pressure of the user's breathing cycle,synchronizes actuation of the PSA phases of operation with the user'sbreathing cycle such that enriched oxygen gas 216 is produced by theVPSA system 306 and collected in the oxygen purge tank 330, and isreleased, e.g., outputted, to the user during the productive portion ofthe user's breathing cycle. As previously described herein, thecontroller 380 dynamically controls the VPSA system 306 such that eachPSA cycle is synchronized to each breath (exhalation/inhalation phasepair) of the user, and such that the actuation timing, PSA phaseduration, flowrate, volume and/or timing of output gas released to theuser can be varied from one PSA cycle to the next, in response tovariation in one user breath to the next, as sensed or otherwisedetermined by the controller 380.

FIG. 3L illustrates an example PSA system 306 which is advantaged bybeing configured such that the VPSA system 306 includes the continuousoperation of one single compressor 316 with no surge tanks, whilegenerating intermittent raffinate product, wherein the raffinate productis an oxygen rich gas 216. During the desorption phase 241 when noraffinate product is being produced, pressurized air supply 236 beingoutput from the continuous air compressor 316 is routed to a venturivacuum generator 318 in order to utilize the pressurized air supply 236as a vacuum source, without requiring a separate vacuum pump. Thisventuri vacuum generator 318 relies on the movement of the pressurizedair 236 into a constricting nozzle. This movement creates an area of lowpressure at the expanding side of the nozzle, also known as the vacuumchamber connection, which pulls nitrogen gas molecules into the flowduring desorption from the vacuum chamber connection, allowing thenitrogen to be exhausted into the atmosphere. This venturi vacuumgenerator 318, which may also be referred to herein as a venturi vacuumchamber 318, may be single stage or multi-stage, and could be utilizedto generate extremely low vacuum pressures. Most molecular sieves forair separation applications such as Lithium X-type zeolite have Type IIisotherms, such that, by creating an extremely low vacuum pressureduring the desorption step 241, a larger portion of the nitrogenadsorption isotherm can be utilized, improving the productivity per gramof adsorbent material and increasing the energy efficiency of the PSAsystem 10. In one example, the venturi vacuum generator 318 is adual-headed diaphragm pump. In one example, other components, includingat least one cooling fan, can be included in a PSA system 10 such as thePSA system 307, to cool components of the PSA system 10.

Referring to the example shown in FIG. 3L, for the adsorption phase 211and similar to that of adsorption phase 211 of the PSA system 300 shownin FIG. 3B, the controller 380 actuates the adsorption phase 211 of thePSA system 307 at the beginning of the inhalation phase and/or at thebeginning of a pre-inhalation period of the exhalation phase precedingthe onset of the inhalation phase, where in one example, the controller380 detects and/or determines the inhalation phase and/or the exhalationphase of the user's breathing cycle using inputs received from one ormore breathing sensors 16, 18. During the adsorption phase 211, valve364 is actuated to connect the output of the continuous compressor 316to the inlet of adsorption column 320 such that compressed air 236 isflowed into the adsorption column 320, where nitrogen in the compressedair 236 is adsorbed into the zeolite material included in the adsorptionbed. The oxygen enriched gas 216, absent most of the nitrogen, flowsfrom the adsorption column 320 to oxygen purge tank 330, resulting in apressure drop across the adsorption column 320. As such, the airpressure at the outlet of adsorption column 320 is higher thanatmospheric pressure during this adsorption phase 211. During theadsorption phase 211, valve 340 is set to an open position, such thatconcentrated oxygen gas 216 flows to the user during the productiveportion of the user's breathing cycle 202.

For the desorption phase 241, and similar to that of desorption phase241 of the PSA system 300 illustrated in FIG. 3E, the controller 380actuates the PSA system 307 to enter the desorption phase 241 during thenon-productive portion of the user's breathing cycle, for example, atthe beginning of the exhalation phase of the user's breath, as detectedand/or determined by the controller 380 on a breath by breath basis.During the desorption phase 241, valves 340 and 364 are each in the“OFF” configuration. In one example, only valve 340 is configured in the“OFF” configuration. Valve 374 connects the inlet of adsorption column320 to the inlet of venturi vacuum generator 318. During the desorptionphase 241, the pressure gradient through adsorption column 320 reversessuch that the outlet is at higher pressure than at the inlet. Due to thesub-atmospheric pressures created by the vacuum generator 318, an oxygenpurge stage is not needed to remove nitrogen from the adsorbent column320. As the pressure in adsorption column 320 decreases, nitrogendesorbs from the adsorbent material in the adsorption column 320, into agaseous state. The pressure gradient causes the gaseous desorbednitrogen to flow out the inlet of the adsorption column 320, throughvalve 374 and the venturi vacuum generator 318, to the nitrogen releaseoutlet, to be exhausted from the PSA system 307. When the controller 380senses that the exhalation phase of the user's breathing cycle 202 isalmost completed, the controller 380 returns operation of the PSA system307 to the adsorption phase 211 and the cycle repeats.

V. Method

FIG. 4 shows an example illustration of a method 400 for controlling anoxygen concentrator including a PSA system 10, as described herein andillustrated by the figures, to output enriched oxygen gas 216 from theoxygen concentrator to a user, where outputting of the enriched oxygengas 216 is synchronized, on a breath by breath basis, with theindividual user's breathing cycle 202. As previously described herein,the breathing cycle 202 of an individual user of an oxygen concentratoris comprised of a series of sequential breaths, such that each breath ispreceded by a preceding breath and followed by a succeeding breath, andsuch that each breath includes an inhalation phase and an exhalationphase. The duration, breathing pressure pattern, oxygen flow rate andvolume, carbon dioxide flow rate and volume, etc. can vary from onebreath to another, such that a normal breathing cycle 202 includesvariation from one breath to another. The method 400 described hereincontrols the operation of a PSA system 10 during each breath of a userusing the oxygen concentrator including the PSA system 10, tosynchronize, for each breath, the output of oxygen enriched gas 216 withthe inhalation and exhalation phases of that breath. As such, each PSAcycle performed by the PSA system can vary from another PSA cycle, forexample, in the duration of each PSA phase 211, 221,231, 241 of the PSAcycle, the volume and/or flowrate of the gases outputted from the PSAsystem to the user during the PSA cycle, which can include, in thevarious example configurations described herein, outputted enrichedoxygen gas 216 and/or outputted pressurized air 236, etc., where itwould be understood that variation of each PSA cycle from another PSAcycle is an essential feature of the control method 400 to enablesynchronization of each PSA cycle with a corresponding breath of theuser's breathing cycle 202.

Referring to the illustrative method 400 shown in FIG. 4, during steps401 to 405 of the control method 400, the oxygen concentrator is in useby the user, e.g., a gas outlet of the PSA system 10 is in fluidcommunication with the user's respiratory system, for example, via anasal cannula 12 connected to the gas outlet of the PSA system 10. Aspreviously described herein, one or more breathing cycle sensors, whichcan include a breathing pressure sensor 16 and/or one or more breathingcycle sensors 18, are operatively connected to the cannula 12 to detectchanges in at least one of the breathing cycle parameters sensed by thebreathing cycle sensors 16, 18. The oxygen concentrator can include, inan illustrative example, an oxygen delivery device 342 which can includethe breather cycle sensors 16, 18 and/or the cannula 12. The data iscollected by the breathing cycle sensors 16, 18, also referred to hereinas breathing cycle parameter data or breathing parameter data, isreceived by a controller 380 of the oxygen concentrator, and used by thecontroller 380, for example, in conjunction with one or more algorithmsfurther described herein, to detect, predict, estimate and/or otherwisedetermine various breathing parameters during each breath of the user'sbreathing cycle, including, for example, the breathing pressure patternof each breath, the time at which the inhalation phase of each breathbegins and the exhalation phase of that breath ends, the volume and flowrate of gases inhaled and exhaled by the user during the breath, the O2and CO2 concentration of the inhaled and exhaled gases, etc. In oneexample, parameter data is collected continuously by the sensors 16, 18,and the controller 380 is configured to continuously received theparameter data and to determine the breathing parameters in real time ornear real time, such that the controller 380 can dynamically control theoperation of the PSA system 10 to synchronize each PSA cycle performedby the PSA system 10 with the corresponding breath of the user in realtime, and on a breath by breath basis. In one example, the controller380 is configured to predict and/or estimate the breathing parametersfor a succeeding breath, such that the controller 380 can control theoperation of the PSA system 10 to synchronize the succeeding PSA cycleperformed by the PSA system 10 with the user's succeeding breath, on abreath by breath basis. In this example, the controller 380 can receiveadditional data from the breathing cycle sensors 16, 18 and/or othersensors in the PSA system 10 which can be used by the controller 380 toincrease the accuracy of the predicted and/or estimated breathparameters determined by the controller 380, for example, via a learningalgorithm, feedforward control, or a combination of these.

At step 401, the controller 380 detects, predicts, and/or otherwisedetermines the beginning time of the next inhalation phase of a user'sbreathing cycle 202. In one example, the controller 380 may determinethe ending time of the a current exhalation phase, which would determinethe beginning time of the succeeding inhalation breath of the user.

At Step 402, an adsorption phase 211 of the PSA cycle for the PSA system10 included in the oxygen concentrator is initiated at a timesynchronized with the beginning of the user's inhalation phasedetermined at step 401. In one example, the PSA system 10 is actuated tobegin the adsorption phase 211 and to output oxygen enriched gas 216 tothe user at the beginning of the user's inhalation phase determined atstep 401. In one example, the PSA system 10 is actuated to being theadsorption phase 211 and to output oxygen enriched gas 216 to the userat the end of the exhalation phase of the breath preceding the beginningof the inhalation phase determined at step 401, for example, theadsorption phase 211 is initiated at the beginning of a pre-inhalationperiod of the exhalation phase, as shown in FIG. 1D. In one example, theadsorption phase 211 is actuated by the controller 380, by actuating oneor more valves and/or an air pressurizing device, such as a compressor210, 310, 312, 316 included in the PSA system 10, to deliverpressurized, e.g., compressed air to an adsorption column 320 of the PSAsystem 10.

At Step 403, the adsorption cycle 211 is synchronized to the user'sbreath, to continue to produce oxygen enriched gas 216 at least throughthe productive portion of that breath. In one example, the adsorptioncycle 211 continues until the beginning of an anatomical dead spaceperiod of the inhalation phase of the user's breath is detected. In oneexample, the adsorption cycle 211 continues until the beginning of theexhalation phase of the user's breath is detected. The adsorption cycle211 is ceased at either the beginning of the anatomical dead spaceperiod or the beginning of the exhalation phase, as determined by thecontroller 380 for the specific configuration of PSA system 10 of theuser's oxygen concentrator, such that minimal or no waste oxygenenriched gas is produced during the non-production portion of the user'sbreath, thus providing an advantage of increased operating efficiency ofthe PSA system 10.

At Step 404, concurrent with ceasing the operation of the adsorptioncycle 211, and depending on the configuration of the PSA system 10 ofthe user's oxygen concentrator, the PSA system 10 initiates an oxygenpurge phase 221 and/or a desorption phase 241, to remove adsorbednitrogen from the adsorption column 320, where the desorbed nitrogen isevacuated as nitrogen gas from the PSA system 10, rejuvenating theadsorption column 320 in preparation for the next adsorption phase 211.The desorption phase 241 continues through the non-productive portion ofthe user's breath, which in one example includes at least the non-usefulperiod of the exhalation phase, and can further include the dead spaceperiod of the inhalation phase. In one example, cessation of thedesorption phase 241 is synchronized with the user's breath, via thecontroller 380, to occur at the beginning of the pre-inhalation periodof the user's exhalation phase.

At Step 405, in some example PSA systems 10, during the time period fromthe cessation of the adsorption cycle 211 during the current breath ofthe user, and until the beginning of the adsorption cycle 211synchronized to the succeeding breath of the user, the PSA system 10 canbe actuated, for example, via the controller 380, to deliver pressurizedair 236 to the user.

The method 400 is performed in a continuous loop, returning to step 401,where the controller 380 determines the breath parameters of thesucceeding breath of the user, including, for example, the time at whichinhalation of the succeeding breath will begin, and at step 402,synchronized with the succeeding breath of the user, actuates the PSAsystem 10 to perform the adsorption cycle 211 to provide oxygen enrichedgas 216 to the user during the productive portion of the succeedingbreath. In this manner, the steps 401-405 and method 400 is repeated foreach successive breath of the user, using breathing parameters which aredetermined for each of the successive breaths by the controller 380,such that the PSA cycle can be dynamically varied for each breath asdetermined by the breathing parameters detected for that breath by thecontroller 380. As such, the method 400 is advantaged by synchronizingproduction and delivery of oxygen enriched gas 216 to the user on abreath by breath basis, such that the adsorption and desorption phases211, 241 of each PSA cycle can be varied in sync with the variationdetected in the particular user breath occurring during the PSA cycle,thereby providing oxygen enriched gas 216 only during the productiveportion of each breath, and not providing, e.g., ceasing production ofor conserving oxygen enriched gas 216 in the PSA system 10 during thenon-productive portion of each breath, increasing the efficiency of theoperation of the PSA system 10, and optimizing desorption of nitrogenfrom the adsorption column 320 during the PSA cycle associated with eachbreath.

VI. Control System

By way of illustration, a typical, e.g., average or expected, breath ofa user includes an inhalation phase having a duration of around 2.0seconds, which includes a useful period of around 1.5 seconds followedby an anatomical dead space period of around 0.5 seconds, and anexhalation phase having a duration of around 2.5 seconds, such that eachbreath of a user is around 4.5 seconds in total duration. As such, atypical, e.g., average or expected user breathing cycle 202 would becharacterized by approximately 13 breaths per minute, corresponding to auser breathing rate of approximately 13 breaths per minute. However,because not all humans have the same breathing cycle 202, and exhibitvariability in breathing rate resulting from variations in the durationof each breath and variation in the duration of each inhalation phaseand exhalation phase of each breath, the PSA system 10 described hereinprovides the user with the advantage of PSA cycle times which aredynamically varied on a breath by breath basis, to synchronize oxygengas output 216 to each breath of the individual user. Also, externalconditions such as altitude, weather, temperature of the individualuser's environment, or specific physical activity or physical conditionof the user, may dynamically vary the oxygen requirements of theindividual user, such that the PSA system 10 described herein would alsobenefit the individual user by dynamically varying the PSA cycle on abreath by breath basis, responsive to changes in the user's environmentand/or changes in the user's oxygen requirements due to, for example,the user's then current physical condition and/or activity level, tosynchronize the oxygen output 216 provided to the user during each PSAcycle to the user's then current oxygen requirements and breathparameters, in real time.

In one example, the PSA system 10 is provided comprising a controller380 that can detect, monitor, and regulate each of the adsorption 211,oxygen purge 221, pressure equalization 231, and desorption 241 phasesof each PSA cycle performed by the PSA system 10, in sync with theuser's breath, even when the breathing parameters of that user's breathvaries from a preceding breath and/or is irregular as compared with anaverage breath of that user's breathing cycle 202. The controller 380,in an illustrative example, can be configured as a microprocessor 814(see FIG. 8) with a memory or a programmable logic control system thatcan regulate each PSA cycle and the oxygen output 216 delivered to theuser from that PSA cycle, according to the real time breathing patternof the user, such that the oxygen output 216 for each PSA cycle ismatched with, e.g., synchronized to, the particular user breathoccurring during the that PSA cycle, to dynamically response to changesand/or breath to breath variation in the user's breathing pattern. Inone example, the microprocessor 814 and memory can collect data from theuser's breathing patterns and predict the next breath and/or thebreathing cycle 202 of the user, where the cumulative data can be usedto increase the accuracy of the predictive algorithms used by thecontroller 380 over time. The control system comprises amicroprocessor-based control system or programmable logic control system380 wherein oxygen output 216 and user breathing patterns are matched.In one example, a continuous flow of the enriched oxygen gas 216 isprovided to the user only during the useful period of the inhalationphase of the user's breath, where the adsorption phase 211 is actuatedby the PSA system 10 during the inhalation phase to provide thecontinuous flow oxygen gas, and the oxygen gas 216 is conserved duringthe anatomical dead space period of the inhalation phase and theexhalation phase, wherein during this conservation period the oxygenpurge phase 221 and/or the desorption phase 241 of the PSA cycle isactuated.

One exemplary method of monitoring, regulating, and matching oxygenoutput 216 in real time with that of a user's individual breathing cycle202 can include having pressure sensors configured within the PSA system10 to measure and record each pressure swing period during theinhalation and exhalation phases of each user breath. The data obtainedfrom the pressure swing period cycles can be aggregated and used topredict the average cycling time of a user's breathing cycle 202, e.g.,the user's average breathing rate. In one example, the PSA system 10 caninclude a plurality of pressure sensors, each configured as a massairflow meter (MAF), such that a pressure sensor can be located at eachvalve of the PSA system 10 to sense the pressure variation at the valveover time, to determine each pressure swing period during operation ofthe PSA system 10.

In one example, one or more pressure sensors are connected to theadsorption column 320 to determine the pressure delta caused by thechange in pressure from the adsorption phase 211 of each PSA cycle tothe desorption phase 241 of that PSA cycle. The data obtained from thepressure delta cycles can also be aggregated and used to predict and theaverage cycling time of a user's breathing cycle 202 based on thepressure delta.

In one example, at least one valve in the PSA system 10 can be aproportional control valve such that a tidal volume of a userrequirement can be predicted based on feedback and data gathered aboutprevious breaths from the user. In this example, the controller 380 ofthe PSA system 10 can control the orifice size of the oxygen outputvalve 340, 540, 640 to change the rate at which oxygen enriched gas 216is output to the user. This proportional control valve can also becombined with a ON-OFF solenoid in order to vary output time the oxygenenriched gas 216 is delivered to the user during the adsorption phase211.

In one example, to initiate performance of the adsorption phase 211 bythe PSA system 10, the user's inhalation pressure can be detected by thecontroller 380 using inputs received from the breathing pressure sensor16, and the PSA system 10 can be actuated by the controller 380 to startthe adsorption phase 211 when the breathing pressure caused by theuser's inhalation reaches a certain threshold or represents a certainmathematical pattern based on signal conditioning. The threshold doesnot necessarily need to a be a positive threshold value but could alsobe a negative pressure value (i.e., a value of −0.05 cm H2O pressure).To prevent false positives, the time derivative of the pressure versustime graph can also be calculated. In such case, if the time derivativevalve is positive, such that when the inhalation pressure reaches acertain threshold pressure value close to zero, the adsorption phase 211is actuated by the controller 380. The desorption phase 241 can betriggered by the controller 380 similarly, by detecting a certainpressure threshold associated with the beginning of a dead space periodof the inhalation phase and/or associated with the beginning of theexhalation phase of the user's breath, which could be determined, forexample, using an algorithm which calculates the time derivative of thebreathing pressure versus time graph. Thus, each PSA cycle of the of thePSA system and the oxygen output flow from each PSA cycle can bedifferent from a previous PSA cycle, where learning algorithms and theaccumulated data collected during operation of the PSA cycle duringpreceding breaths can be used to predict the optimal PSA cycle times forthe next PSA cycle, based on previous cycles. In one example, the dataand feedback used by the controller 380 can be lag time, adsorptionkinetics or valve hysteresis that cause time variations in syncing thePSA cycle and oxygen output 216 with each breath of the user and/or theuser's breathing cycle 202.

In one example, the controller 380 can utilize the pressure sensors 16,18 of the oxygen delivery device 342, for example, to detect the user'sinhalation phase based on a negative trigger pressure threshold. Forexample, the threshold can be 0.6 cm H2O pressure. In one embodiment,unless more than the threshold amount of pressure difference is reached,the controller 380 will not trigger an adsorption 211 or desorption 241phase to prevent accidental oxygen bursts or false positives, as suchfalse positives could comprise a pneumatic oxygen delivery system orconserver. In another embodiment, no pressure thresholds are used, butrather time based control with error compensation is employed in thecontrol strategy, configured as an electronic oxygen delivery system orconserver.

In another example, the rate and volume of enriched oxygen output 216that leaves the oxygen purge tank 330 can be adjusted in real time byadjusting the power delivery to the compressor 310. The power adjustmentcan be controlled by the controller 380. In an alternate embodiment,valve 340 can be a variable and/or proportional control valve such thatvalve 340 can be adjusted to allow oxygen output 216 from the oxygenpurge tank 330 at various flowrates.

In one example, the control system for regulating and executing thepressure swing adsorption cycles could mature, e.g., evolve and/orimprove in predictive accuracy over time and with feedback on eachbreath of the user's breathing cycle 202. The feedback can be aggregatedvia the controller 380 to build a time derivative pressure curve definedby the cumulative preceding breaths of the user and measurements of thePSA cycles associated therewith. In one example, the control strategydeveloped using the feedback data can include the PSA system 10controlling each PSA cycle to switch from the adsorption phase 211 tothe oxygen purge phase 221 at a time when the derivative of the pressurecurve reaches a certain negative value. In a non-limiting example, thisnegative value will be defined by the anatomical dead space period ofthe user's inhalation phase, where the negative value may correspond tothe beginning time of the anatomical dead space period, or another timedefined by the anatomical dead space period. Similarly, control strategydeveloped using the feedback data can include the PSA system 10controlling each PSA cycle to trigger the desorption phase 241 when atime derivative of a pressure curve reaches a certain positive value. Inone example, the certain positive value can be defined by the exhalationphase of the user's breath, where the certain positive value correspondsto the start of the exhalation period in one example, and to anothertime defined by the exhalation period in another example. The use oftime derivative pressure curves can allow near instantaneous, e.g., nearreal time, cycle time adjustments for the cycle times of each phase 211,221, 231, 241 of the PSA cycle. In some embodiments, feedforward controlcan be used to compensate for error in oxygen output and delivery overthe course of a user's breathing cycle 202 consisting of a plurality ofbreaths.

Referring to the PSA system 303 shown in FIG. 3H, in an illustrativeexample, when this initial pressure value is reached, the adsorptionphase 211 is actuated by opening valve 360 (two-way valve) to allowcompressed air 236 to flow to the adsorbent column 320. During thisadsorption phase 211 the nitrogen purge valve at the inlet, valve 370,is closed. In one embodiment, valves 360 and 370 may be combined into athree-way solenoid. During this adsorption phase 211, valves 340 and 350are open. Valve 340 can be a proportional control exhaust valve suchthat a tidal volume of the user can be predicted, and oxygen output 216can be precisely output to the oxygen delivery device 342 throughout theuser's inhalation phase in, for example, a sinusoidal manner byutilizing the proportional control exhaust valve 340 such that theorifice size adjusts in order to change the rate at which oxygen isoutput to the user. This proportional control exhaust value could alsobe combined with an ON-OFF solenoid in order to vary different periodsof the adsorption phase 211. In one example, the valve 340 can bereplaced by a two-way solenoid valve in which oxygen can be output in aconstant continuous flow manner during the user inhalation phase.

In the example, the control schema implements feedback control such thatoxygen output volume can be precisely metered per breath by adjustingcompressor 310 airflow output. Proportional-integral-derivative control(PID control) can also be used as a form of feedback control to reducesteady state error associated with precisely delivering oxygen duringthe useful period of the user inhalation phase and conserving oxygenduring the anatomical dead space period of the inhalation phase and theexhalation phase. In one example, PID control of the orifice size of thevalve is adjusted every 1-5 milliseconds using a stepper motor toactuate the proportional control exhaust valve 340. This feedback or PIDcontrol can have adjustment times shorter or longer than 1 milliseconddepending on the sampling rate or frequency of the valve or sensorsincluded in the control schema. This proportional control valve 340outputs the oxygen linearly. The orifice size changes the rate at whichthe oxygen gas 216 is output causing the changing the slope of the line206 as illustrated in FIGS. 1G and 1H. The time derivative of theinhalation pressure versus time graph can be used to determine theinstantaneous rate of oxygen output required during inhalation at acertain moment in time. This positive time derivative valve can becorresponded with the slope of the proportional control valve 340output. By adjusting this orifice size every few milliseconds duringinhalation, creating a sum of linear equations, the actual oxygen outputfrom the proportional control valve 340 can accurately approximate thepressure versus time graph. PID control can be used to continuouslycalculate the steady state error and adjust the linear equations toreduce the steady state error over time and with each succeeding breathof the user's breathing cycle 202.

In another example, the controller 380 can use a sinusoidal function toapproximate a user's breathing pattern. While the computations can beintensive in creating the exact mathematical function, sinusoidalfunctions can be approximated computationally faster with low percenterror using a Taylor polynomial expansion such that the degree of thepolynomial n can be determined based on lag time and accuracy requiredfor the PSA systems 10 described in FIGS. 3A-3K. As the degree of thepolynomial n increases, the accuracy increases. In one example, thefeedback control involves using pulse width modulation (PWM) controlsuch that the compressor 310 airflow output can be changed per PSAcycle, e.g., on a breath by breath frequency, by adjusting the dutycycle or frequency of the pulse wave.

Using pressure sensor data, a pressure versus time graph can begenerated. The time derivative of this pressure versus time graph can becalculated and, once a certain negative time derivative value is reachedand the pressure detected is positive, valve 340 will fully close, andthe PSA cycle will enter the oxygen purge phase 221. During this step,valves 350 and 360 will still be open and valve 370 will still beclosed.

Referring again to the example PSA system 202 shown in FIG. 3H, duringthe desorption phase 241, the control system 380 determines that theactual pressure values are negative, and when the time derivative of thepressure versus time graph reaches a certain negative value, actuatesvalves 360 and 340 to close and actuates valves 350 and 370 to open. Inone example, the controller can be configured to have default settingfor the oxygen flow cycles. The setting can be set, for example, at 15breaths per minute when the PSA system is turned on. The controller canbe configured to start the inhalation period and adsorption phase onlywhen the pressure sensor reaches a certain threshold. In one example,the pressure threshold can be based on a negative threshold pressure,such as −0.06 centimetre of water (cmH2O). The controller 380 candynamically change the rate of each PSA cycle time and as well as thetime for each PSA phase 211, 221, 231, 241, depending on the breathingpattern of the user, on a breath by breath basis. Alternatively, thecontroller 380 can also configure the PSA system to not deliver oxygenwhen pressure sensor detects that the user is not inhaling air or thereare other failed triggers that do not justify delivering the enrichedoxygen gas 216 to the user. The default setting for a particular usercan also change based on the user's specific breathing pattern usingmulti-predictive controls executed by the controller 380.

VII. Rapid Pulsed Pressure Swing Adsorption System

In one example, a rapid type pulsed pressure swing adsorption system(RPPSA system) is provided. The RPPSA system is an example of a pulsedpressure swing adsorption system 10. As illustrated by the phase graph20F shown in FIG. 1J, an RPPSA system 10 can operate using one adsorbentcolumn 320 and a pressurized air source 310, such that the cycle timesof the PSA cycle of the RPPSA system 10 are faster than, e.g., ofshorter duration than, the physiologically useful phases of respiration(generally less than 2 seconds). In this embodiment, oxygen pulses areproduced one or more times during the physiologically useful phases ofrespiration, e.g., during the useful period of the inhalation phase and,in some embodiments, during the pre-inhalation period of the exhalationphase, of a user's breath. In some embodiments, and as shown in theexample phase graph 20F, during the inhalation and exhalation phases, attimes when oxygen enriched gas 216 is not being output during,pressurized air 236 can be output to the user, in order to increase FiO2levels in the user, as compared to natural aspiration with nopressurized air 236 being provided to the user. Further, in someembodiments, a positive end expiratory pressure (PEEP) can be providedby a pressurized air source 310 during the phases of user breathingwhich are not physiologically useful and/or when no oxygen gas 216 isbeing output to the user, such as during the non-useful period of theexhalation phase and during the anatomical dead space period of theinhalation phase of a user's breath.

In one example, the RPPSA system 10 includes one or more adsorbent bedsin a pulsed PSA system 10 that generates raffinate product, such asenriched oxygen, non-continuously, e.g., in discrete pulses of enrichedoxygen gas 216. These non-continuous oxygen pulses 216 are outputtedduring the adsorption phase 211, when pressurized air 236 enters themolecular sieve adsorbent bed and is separated by adsorption of thenitrogen by the adsorbent, resulting in production of a raffinateproduct, e.g., producing a raffinate product, which in the example of anoxygen concentrator disclosed herein, is an oxygen concentrated gas 216.This RPPSA system 10 alternates in operation between the adsorptionphase 211 (also indicated as “A” in FIG. 1J), and a desorption phase 241(also indicated as “D” in FIG. 1J), wherein during the desorption phase241, oxygen enriched gas 216 is not being output and nitrogen is beingdesorbed from the molecular sieve adsorbent bed 955. The PSA cycle timesof this rapid pulsed pressure swing adsorption system 10 are variableand defined in real time on a breath by breath basis, by the user'sbreathing rate to determine the inhalation and exhalation cycles of theuser. In this example, the output of oxygen enriched gas 236 to the usercan be precisely adjusted to the user's requirements and breath flowphases individually for each breath taken by the user, e.g., on a breathby breath basis, using one or more of adjustments made to the PSA cycletimes for the various PSA phases 211, 221, 231, 241, the user's measuredbreathing pressure 16 and/or breath rate, and a blower flowrate output,which in one example can be adjusted by varying the level of powersupplied to the blower 14 or microblowers 816.

The RPPSA system 10 can incorporate components such as thin adsorbentbeds 755, 955 to limit kinetic resistance, high volumetric flow lowpressure changes blowers that allow higher product gas flow and maintainproduct gas purity, and ultra-rapid cycle times greater than 2 Hz toimprove the productivity of the thin adsorbent bed 755, 955. In oneexample, microblowers 816 are used to create an ultra-thin oxygenconcentrator device wherein cycle times of above 10,000 Hz are possible,as illustrated by the example shown in FIGS. 7A-12. The URPSA systemconfiguration 700, 900 can be utilized with different adsorbentmaterials to provide a PSA system 10 which is advantaged by compact sizeand packaging, user convenience and portability, and efficiency ofoperation, This ultra-rapid pressure swing adsorption (URPSA) system700, 900 can be used not just for producing an oxygen enriched gas 216,but also with different adsorbent materials. pressure swing adsorptionsystems 10 for the production of gas species such as nitrogen, hydrogen,methane, etc.

In the examples shown in FIGS. 7A-12, the RPPSA system 700, 900 is asingle bed ultra-rapid pressure swing adsorption (URPSA) system that hasultra-rapid PSA cycle times, in some cases greater than 2 Hz. The use ofultra-rapid PSA cycle times allows for the PSA system 700, 900 to bereduced in size and increases the energy efficiency by the reducing thetotal amount of zeolite adsorbent required to create the same amount ofproduct gas as compared to a PSA system operated with slower PSA cycletimes. Further, by using ultra-rapid PSA cycle times, it is possible togenerate “quasi-continuous” raffinate product, eliminating the need formultiple adsorbent beds in pressure swing adsorption applications wherecontinuous product output is necessary.

In this example, a pancake-like thin zeolite adsorbent bed 755, 955 witha length to diameter ratio, or L/D, of less than 1:1 is utilized. Thisallows the pressurized inlet gas 236 to linearly diffuse through theadsorbent column faster than high L/D adsorbent beds while also limitingaxial diffusion and reducing pressure drop across the adsorbent bed 755,955.

In this example, by allowing the RPPSA system to utilize lower pressureratios, i.e. 1.2:1, with thin adsorbent beds 755, 955, higher volumeand/or higher purity product gas can be produced at lower incoming airpressures. This oxygen product gas 216 can be produced at a purity levelsuch the oxygen product gas 216 having an oxygen output pressurepotentially as low as 4 cmH2O, nearly matches a user's breathingpressure demand. This allows low pressure, higher volume oxygen outputto be produced from a PSA system 10 using centrifugal air blowers suchas those used in CPAP machines, which produce less than 100 cmH2O airpressure, rather than prior art oxygen concentrator air compressorswhere the pressurization is over 1000 cmH2O air pressure. This lower O2pressure output is useful since mass flow of O2 is much more importantthan pressure for gas exchange and PaO2 saturation during respiration,especially given that emphysema (COPD) patients have lower lungcompliance than normal people, and hence the elastic forces required toopen alveoli to create useful gas exchange in lungs is much less thanthe higher pressure oxygen output from prior art oxygen concentrators.Further, lower pressurization ratios in some embodiments of RPPSA allowfor much higher energy efficiencies compared to prior art PSA systems,since less energy is required to compress the input air, hence watts ofpower consumption per liter per minute of oxygen produced is decreasedsubstantially, potentially to one-tenth the power consumption of priorart PSA systems.

Further, the velocity of the compressed air 236 is related to thepressure ratios utilized, and the velocity of air is inverselyproportional to the time exposure to the adsorbent material. Hence, withthin adsorbents 755, 955, where the mass transfer constant k is a largevalue, it is undesirable to utilize high pressures since that wouldlimit the time exposure of the air to the adsorbent material, hencereduce product gas (in this example, O2 gas) purity and output. Thepresent disclosure seeks to solve this problem through the creation ofan RPPSA system that can facilitate ultra-rapid pressurizations anddepressurizations in a thin profile package, with the use of lowerpressure ratios in conjunction with thin adsorbent beds 755, 955.Further, since pressure and volume are fundamental tradeoffs incompressor design and/or selection, with lower pressure ratios it ispossible to utilize compressors and/or blowers that have high input gasvolume flowrates, increasing product gas output.

The example of a thin-bed structure of the adsorbent material isnon-limiting. For example, in one embodiment, structured adsorbents withlow pressure drop could be utilized. These structured adsorbents couldcomprise foams, laminates, 3D printed adsorbents, honeycombs, and/orhighly spherical or patterned adsorbent beads. Further, these adsorbentscan be a thin layer of LiX zeolite pellets or a monolithic structurewith a length to diameter, or L/D ratio, of less than 0.1 for example,to facilitate rapid mass transfer, improve adsorption kinetics, andminimize pressure drop during ultra-fast adsorption and desorptioncycles. The activated alumina or silica gel is meant to adsorb watervapor and carbon dioxide, which in small concentrations can over timereduce the nitrogen adsorption performance of the LiX zeolite adsorbent.

In one example, a very thin ultra-rapid pressure swing adsorption system700, 900 can be built using microblowers or micropumps 816, which in oneexample are arranged in a microblower array 810. In one embodiment, thefeed air is pressurized using piezoelectric microblower(s) 810. Thesepiezoelectric microblowers 816 have a thin profile and utilizeultrasonic 26 kHz vibration of a piezoelectric ceramic material, forexample, to discharge air from the microblower 816 at a gauge pressureabove 1.9 kPa. Further, the ultra-rapid low-pressure swing adsorptionsystem 10 utilizes one or more rapid actuating valves such aspiezoelectric or solenoid valves to produce rapid adsorption anddesorption cycles, having ultra-rapid cycle times which in someembodiments range from about 10 Hz to about 10,000 Hz. The piezoelectricmicroblowers 816 are positioned in the URPSA system 700, 900 next to themonolithic adsorbent material and blow pressurized air toward theadsorbent material, with the one or more valves on one side of theadsorbent, rapidly actuating to depressurize the system via anatmospheric purge, and micro-sized air blowers 816 on the opposite sideof the absorbent material to evenly distribute the pressure from thepiezoelectric microblowers 816 across the entire adsorbent monolith.

In one embodiment, this ultra-rapid pressure swing adsorption could beused to produce medical oxygen. In one example, the single adsorptionbed and pulsed pressure swing adsorption process allows the PSA systemto quasi-continuously produce oxygen product gas during inhalation viathe ultra-rapid cycle times and then conserve oxygen during exhalationby implementing a longer purge cycle time or longer desorption phasecycle time.

A. RPPSA with Multiple Valves and Oxygen Purge Tank

Referring to FIG. 5, shown is an example pressure swing adsorption (PSA)system 500 which generates raffinate product such as enriched oxygen gas216 non-continuously, in rapid pulses, such that the PSA system 500 canbe characterized as a rapid pulse PSA (RPPSA) system 500. Themicroblowers 510, 610 described in both FIGS. 5 and 6 are used tofacilitate ultra-rapid type pressurization and vacuum depressurizationof gas and air in the RPPSA system 500. In this configuration, themicroblowers can cause cycle times of 10,000 Hz with a low-pressuregradient which allow for rapid PSA cycles. This process allows for afaster oxygen purge 221 and desorption 241 phases in the pressure swingadsorption cycle.

In this example, the PSA system 500 comprises at least one microblower510, an adsorption column 520, and an oxygen purge tank 530. Thecompressor 510, adsorption column 520, and oxygen purge tank 530 can beconnected to each other in series, and shown in FIG. 5. A valve 560operably connects the microblower 510 to the adsorption column 320 andacts as a gate for either allowing or blocking gas to flow from themicroblower 510 to the adsorption column 520. The PSA system 500 canalso include a controller 580 which can monitor and control the amountand direction of flow of the gases by selectively controlling the powerdelivered to the microblower 510, valve 560, and/or valve 540. In oneexample, valve 540 is a two-way solenoid valves and valve 560 is a 3-waysolenoid valve. In this example, the adsorption column 520 can include athin, pancake-like, zeolite adsorbent with a length to diameter (L/d)ratio of less than 1:1. In this example, the microblower 510 can be anarray of piezoelectric microblowers embedded on a printed circuit board(PCB), such as the array 810 of microblowers 816 shown embedded on aprinted circuit board 800 shown in FIGS. 8 and 11.

In one example, the controller 580 can actuate the PSA system 500 toenter into the adsorption phase 211 at a selected one of the beginningof the user's inhalation phase, slightly before the beginning of theuser's inhalation phase such as during a pre-inhalation period of theexhalation phase preceding the inhalation phase, or slightly after thebeginning of the user's inhalation phase depending on the control schemaused. During this adsorption phase 211, valve 560 is set open, toconnect the output of microblower 510 to the inlet of adsorption column520, and valve 570 is closed. At this point, the microblower 510receives atmospheric air, pressurizes the atmospheric air to createpressurized air 236, and outputs the pressurized air 236 through thevalve 560 to the inlet of adsorption column 520. In one example, thepressurized air 236 has an air pressure which is greater than 1atmospheric pressure. The adsorption column 520 contains zeolite whichadsorbs the nitrogen from the pressurized air 236 to produce a raffinatewhich is an oxygen enriched gas 216. At this point, valve 570 is closedin an “OFF” position. The oxygen enriched air 216, absent most of thenitrogen, flows from the adsorption column 520 to the oxygen purge tank530, with a resultant pressure drop across the adsorption column 520.Pressure in oxygen purge tank 530 is only slightly higher thanatmospheric pressure during this adsorption phase 211. Valve 540 is alsoset to open such that the oxygen enriched gas 216 flows from oxygenpurge tank 530 to the user.

In one example, the microblower 510 is not set to output a constantamount of pressure. Rather, the controller 580 dynamically adjusts theair pressure and flowrate output from the microblower 510 in order tochange the oxygen output 216, on demand as needed to meet the userrequirements for oxygen output 216 defined by the breath flow phases ofthe user's breath. The adjustment in air pressure and flowrate output ofthe microblower 510 can occur on a breath by breath basis, to adjust tobreath to breath variations in the user's breathing cycle 202.Adjustment of the microblower 510 air pressure and/or flowrate outputmay be required because the pressure difference required to perform theadsorption phase 211 is variant upon the breathing pressure from auser's inhalation phase as well as the porosity (adsorption capabilityof the filter) of the filter, which can change from breath to breathand/or over time, for example, based on the condition of the adsorbent.The controller 580 can adjust the microblower 510 using feedback controlsuch that the microblower 510 operation may be adjustable evermillisecond or less, depending on the sampling frequency utilized byanalog or digital control sensors in the PSA system 500 and/or an oxygendelivery device 342 connected to the PSA system in use.

In a next step, the controller 580 actuates the PSA system 500 to enteran oxygen purge phase 221, during the dead space period of theinhalation phase. Valve 560 remains set to open, to connect the outputof the microblower 510 to the inlet of adsorption column 520. Valve 540is now switched to closed in an “OFF” position, preventing flow ofenriched oxygen gas 216 from the oxygen purge tank 530 to the user. Asconcentrated oxygen 216 flows from the adsorption column 520 into theoxygen purge tank 530, pressure in oxygen purge tank 530 increases,although it remains less than the pressure of air entering adsorptioncolumn 520.

In one example, the microblower 510 can be set to an always “ON”position such that the microblower 510 is constantly outputtingpressurized atmospheric air 236 through its outlet. During the oxygenpurge phase 221, the pressurized air 236 from the microblower 510 willflow out of the PSA system 500 back into the atmosphere without firstentering the adsorption column 520.

Following the oxygen purge phase 221, the controller 580 actuates thePSA system 500 to enter the desorption phase 241 during the user'sexhalation phase. During the desorption phase 241, valve 540 remainsclosed. Valve 560 is configured to allow the pressurized air 236 fromthe microblower 510 to directly release out of the PSA system 500, backinto the atmosphere. Valve 570 is opened in an “ON” position allowingflow of gas from the adsorption column 520 to the atmosphere. Valve 340remains closed in an “OFF” position since during the exhalation phase,the user does not have a requirement for enriched oxygen gas 216. Duringthe desorption phase 241, the pressure gradient through the adsorptioncolumn 520 reverses such that the outlet is at higher pressure than atthe inlet of the adsorption column 520. As the pressure in theadsorption column 520 decreases, nitrogen desorbs from the zeoliteadsorbent, e.g., re-enters the gaseous state. The pressure gradientcauses the air in the adsorption column 520, including the desorbedgaseous nitrogen, to flow out the inlet of the adsorption column 520,through valve 570, to release the desorbed nitrogen gas from the PSAsystem 500 and back into the atmosphere. Some concentrated oxygen flowsfrom oxygen purge tank 530 back into adsorption column 520 throughpressure equalization. When the controller 580 senses that the user'sexhalation phase is almost completed, the controller 580 actuates thePSA system 500 to return to the adsorption phase 211 and the PSA cyclerepeats.

B. RPPSA with Single Valve

FIG. 6 illustrates a rapid pulse PSA (RPPSA) system 600 similar to thatof PSA system 500 of FIG. 5. As illustrated in FIG. 6, the RPPSA system600 comprises at least one microblower 610 and an adsorption column 620.The microblower 610 and adsorption column 620 can be connected to eachother in series. The PSA system 600 can also include a controller 680which can monitor and control the amount and direction of flow of thegases by controlling the microblower 610 and a two-way valve 640. Inthis example, the adsorption column 620 can include a thin,pancake-like, zeolite adsorbent with a length to diameter (L/d) ratio ofless than 1:1. In this example, the microblower 610 can be an array ofpiezoelectric microblowers, such as the array 810 of microblowers 816shown embedded on a printed circuit board 800 shown in FIGS. 8 and 11.

In one example, microblower 610 is not set to a constant amount ofpressure, as the pressure difference required at a given time is variantupon the breathing pressure from a user's inhalation phase at that time,as well as the porosity (adsorption capability of the filter) of thefilter, which can change from one PSA unit to another due, for example,manufacturing variation of the filter. In one example, the controller680 can adjust the air pressure and flowrate output from the microblower610 in order to change the oxygen output 216, depending on userrequirements and/or the user's breath flows and/or breathing cycle 202detected by the controller 680. In one example, the controller 680 canadjust the microblower 610 pressure and/or flowrate output usingfeedback control, such that the microblower 610 pressure and/or flowrateoutput is adjustable every millisecond or less.

In one example, the microblower 610 is bidirectional such that themicroblower 610 can be configured to deliver atmospheric and pumppressurized air 236 into the adsorption column 620 in one direction, andin the other direction operate to draw air from the adsorption column620 during the desorption phase 241 of the PSA cycle. In one example,this microblower 610 could comprise a singular or array of fans,blowers, centrifugal, or diaphragm pumps such that high volumetric airflow and low pressurization are produced. For example, using thisconfiguration, less than 1.4 atmospheres of pressurization can begenerated from the blower 610. In one example, these changes in pressurecould be ultra-low wherein 2.1 mmH2O of gauge pressure is produced,allowing for high volumetric flowrates and with ultra-low pressure dropadsorbent materials. In another example, the microblower 610 comprisesan array 810 of microblowers 816 such that some of the microblower areconfigured to intake atmospheric air, pressurize the air, and deliverthe pressurized air to the adsorption column 620 to actuate adsorptionof nitrogen from the air 236, thus producing an oxygen enriched gas 216,and some of the microblowers 816, shown collectively in FIG. 6 as avacuum blower 612, are configured in the reverse direction to flow airfrom the adsorbent such that nitrogen is desorbed from the adsorbent andvented as gaseous nitrogen back into the atmosphere during a desorptionphase 241 of the PSA cycle. In this case, during the oxygen purge phase221 and the desorption phase 241, the reverse microblowers 816 of themicroblower array 810 are actuated, e.g., powered on and intake thenitrogen and excess oxygen from the adsorption column 620 and releasethe gases back into the atmosphere back in the direction from where theatmospheric air came from in the adsorption phase 211. In one example,during the oxygen purge 221 and desorption 241 phases, the microblowers810 shut off and the solenoid valve shuts off. In one example, theinternal pressure of the zeolite adsorbent pushes nitrogen back out,causing the nitrogen to desorb as a gas. In one example, the reversemicroblowers 810 are selectively turned on to speed up the pressureequalization phase 231, e.g., decrease the pressure equalization phasecycle time, in addition to the flow of air from the internal pressure ofthe zeolite.

In one example, the microblowers 610, array 810 are controlled by aMOSFET switch 812 or some other type of microcontroller 814 that canregulate voltage of the MOSFET 812. In this example, only one solenoidor piezoelectric valve is required in order to facilitatedepressurization and pressurization, along with production of output gas216. With piezoelectric microblowers 816, it is possible to shut eachindividual microblower 816 or microblower array 810 ON or OFF extremelyrapidly using MOSFET switches 812. For example, a pulse width modulationcontrol can simulate a 26 kHz square wave form of the piezoelectricmicroblowers 816, precisely controlling the piezoelectric oscillationsin order to turn the microblowers 816 ON or OFF without any partialoscillations, thus allowing full depressurization and pressurizationcycles within the PSA system 600, even at extremely rapid cycle times.

VIII. Exemplary Ultra-Rapid Pressure Swing Adsorption System

In one example, provided is an example PSA system 700 similar to that ofthe PSA system 600 of FIG. 6. In this example, as illustrated in FIGS.7A-B, a small form factor PSA system 700 is configured to provideenriched oxygen 216 to a user, where the small form of the PSA system700 is advantaged by being lightweight and portable for the convenientof the user.

As illustrated in FIGS. 7A-7B, provided is a PSA system 700 shown in anexploded perspective view. FIG. 7A illustrates the PSA system 700 in anexploded perspective top view and FIG. 7B illustrates the PSA system 700in an exploded bottom view. As illustrated in FIGS. 7A-7B, a number oflayers of components are combined to form the PSA system 700. In oneexample, provided is a Printed Circuit Board (PCB) 710 including amicroblower array 810 comprised of a plurality of microblowers 816embedded on the PCB 710. The PSA system 700 also includes a filter 720and a filter frame 730 configured to separate the PCB 710 from contactof the adsorbents, which in the present example are configured as a bed755 of zeolite pellets. In one example, the filter 720 is a mesh orsheet metal to protect the PCB 710 from contact with the zeolite bed 755and to prevent any particles other than air from reaching the zeolitebed 755. In an example shown in FIG. 10, the filter 720 is supported inthe PSA case 750 by a plurality of rails 732, spaced so as to notinterfere with air flow through the adsorption cavity defined by the PSAcase 750. The filter 720 is in a mesh shape to allow pressurized airfrom the PCB 710 to diffuse through the filter 720 and reach the zeolitecomprising the adsorption bed 755. Further, in another example, anelectrostatic filter can be placed on one or more portions of the PCB710 to reduce dust accumulation in the PSA system 700 and hence increasethe lifecycle of the microblower array 810. Below the filter 720 is acase 750 for the PSA system 700. A cavity defined by the case 750 housesan adsorption bed 755 configured to store adsorbent material such aszeolite pellets. The adsorption bed 755 is thin and has a length todiameter ratio of about 1:1. The adsorption bed 755 and support rails732 (see FIGS. 10-12) are configured to allow the filter 720 and PCB 710to rest above the adsorption bed 755 such that the zeolite in theadsorption bed 755 is prevented from coming in contact with either ofthe filter 720 and the PCB 710. A top frame 740 is configured to fitsnugly inside an outer portion of the case 750. The frame 740 and case750 is configured in a way that the frame 740 and case 750 will sandwichthe PCB 710 and filter 720 in a fixed position so that PCB 710, filter720, and any zeolite pellets in the adsorption bed 755 are in a lockedposition relative to each other.

At a bottom portion of the case 750 is a circular shaped divotcomprising a nozzle 770 configured to receive a valve 760, such as asolenoid valve. The nozzle 770 is configured to connect the valve 760 tothe PSA system 700. The solenoid valve can receive and release enrichedoxygen 216 that is filtered in the PSA system 700 through the thinzeolite mesh bed 755. The valve 760, similar to that of valve 640 ofFIG. 6, is configured to regulate the flow of oxygen enriched gas 216from the PSA system 700 to the user. The nozzle 770 also comprises arelease portion for oxygen to flow from the PSA system 700 to the userwhen the valve 760 is configured in an “ON” position.

FIG. 8 illustrates a more detailed view of the PCB 710 of FIGS. 7A and7B, where in the example illustrated in FIG. 8, the PCB 710 isconfigured as a Printed Circuit Board (PCB). The PCB 800 includes amicroblower array 810, a MOSFET switch 812 configured to regulate thevoltages of the microblower array 810, effectively regulating the amountof pressurized air flowing in and out of the piezoelectric microblowers816 of microblower array 810. The PCB 800 also includes microcontrollers814 and microprocessors to regulate the valve 760, microblowers 816,MOSFET 812, and to provide power to the other components of the PCB 800.

In this example, there can be any number of microblowers 816 in themicroblower array 810. In one example, the microblowers 816 areconfigured in a grid pattern. In one example, USB power supply (notshown) can be configured to power the PCB 800 and its componentsincluding the microprocessors 814 and microblower array 810. In oneexample, on the reverse side of PCB 800 (see FIG. 7B) are another set ofmicroblower arrays 810 facing the opposite direction. The reverse set ofmicroblowers 810 serve the purpose of moving air, particularly nitrogenfrom the zeolite chamber bed 755 back into the atmosphere during adesorption phase 241, where the nitrogen rich air is moved in adirection opposite the air flow generated by the microblower array 810operating during the adsorption phase 211. In one example, both sets ofmicroblower arrays 810 are on mounted on the same side of the PCB 800,with at least one array 810 operable to move desorbed air away from theadsorbent bed 755, and at least one array 810 operable to moveatmospheric air to the adsorbent bed 755 during an absorption phase 211.

In this example, the microcontroller 814 synchronizes actuation of thedesorption phase 241 of the PSA system 700 with the exhalation phase ofthe user's breathing cycle, such that during the desorption phase 241the microblowers 816 will blow in a reverse direction, e.g., will blowair away from the adsorption bed 755, causing a vacuum-type desorptionof the adsorption bed 755, during which nitrogen desorbed from theadsorption bed 755 and any excess enriched oxygen gas 216 will flow inthe opposite direction of the air flow from the adsorption phase 211,through the filter 720 and through the PCB 710 via the microblower array810, to be released back into the atmosphere.

FIGS. 9A-9D illustrate an example PSA system 900 similar to that of theexample PSA system 700 of FIGS. 7A-B. FIG. 9A shows a partial sectionalperspective view of the PSA system 900 in an assembled state,illustrating the thin profile and compact packaging of the PSA systems700, 900 and including a filter frame 930, a filter 920 and a printedcircuit board (PCB) 910 layered in a case 950 and retained in the case950 in the layered arrangement by a frame 940. The filter 920 functionsas described for the filter 720 of the PSA system 700 shown in FIGS.7A-7B, to prevent particles other than air from migrating from theadsorbent bed 955 to the PCB 910 and/or the microblower arrays 810, andto prevent particles other than air from migrating from the atmosphere,via the microblower arrays 810, to the adsorbent bed 955. As shown inFIG. 9A, the adsorbent bed 955 is positioned in a cavity defined by thecase 950 such that atmospheric air blown by the microblower arrays 810onto the adsorbent bed 955 during an adsorption phase 211 can react withthe adsorbent bed 955, to absorb nitrogen from the atmospheric air andto produce oxygen enriched gas 216 which can be released from the cavityof the PSA case 950 via a release nozzle 970 and/or a valve 960. In oneexample, the microblower array 810 is bidirectional such that themicroblower array 810 can be configured to operate in a first directionto intake atmospheric and pump pressurized air 236 into the adsorptionbed 955 via the filter 920 during an adsorption phase 211, and tooperate in a second direction to draw nitrogen gas desorbed from theadsorption bed 955 during a desorption phase 241 out of the case 950 viathe microblower array 810. As previously described herein themicrocontroller 814 of the PSA system 900 can be configured to detectthe inhalation and exhalation phases of a user's breathing cycle 202,and can be further configured to synchronize actuation of one or more ofthe various phases 211, 221, 231, 241 of the PSA cycle with the user'sinhalation and exhalation phases, on a breath by breath basis.

In one example, the microblower array 810 could comprise a singular fanor array of fans, blowers, centrifugal pumps, diaphragm pumps or acombination of these, wherein high volumetric air flow and relativelylow pressurization of the air moved by the microblower array 810 isproduced. This could mean, for example, less than 1.4 atmospheres ofpressurization from the blower array 810. These changes in pressurecould be ultra-low, such that about 2.1 mmH2O of gauge pressure isproduced, allowing for high volumetric flowrates and the use ofultra-low pressure drop adsorbent materials. In another example, amicroblower array 810 can comprise a plurality of microblowers 816 suchthat some of the microblowers are configured to intake atmospheric air,pressurize the air, and deliver the pressurized air 236 to theadsorption bed 955 and some of the microblowers are configured to moveair in the reverse direction to intake the nitrogen desorbed from theadsorbent bed 955 and release the gaseous desorbed nitrogen back intothe atmosphere during a desorption phase 241 of the PSA cycle performedby the PSA system 900. In one example, a solenoid valve or series ofsolenoid valves could be used to replace the microblowers 816 tofacilitate vacuum depressurization, as illustrated in the PSA system 700shown in FIG. 10. In this example, during the oxygen purge phase 221 andthe desorption phase 241, the reverse microblowers 816 of microblowerarray 810 are turned on and intake the nitrogen and excess oxygen fromthe adsorption bed 755 and releases the gases back into the atmospherein a direction opposite from the where the atmospheric air was taken induring the adsorption phase 211.

In one example, during performance of the oxygen purge 221 anddesorption 241 phases of the PSA cycle, the microblowers 816 shut offand the solenoid valve 760 shuts off In one example, the internalpressure of the zeolite pushes nitrogen back out, e.g. causes adsorbednitrogen to desorb from the adsorption bed 755, 955 in a gaseous form.In one example, the reverse microblowers 816 can be powered on to speedup the pressure equalization phase 231, in addition to flowing air fromthe adsorption bed 755, 955 during the desorption phase 241.

In one example, as shown in FIGS. 8 and 9B, the microblowers 816 and/orthe microblower arrays 810 are controlled by MOSFET switches 812 or someother type of microcontroller(s) 814 that can regulate voltage of theMOSFET 812. In this example, one solenoid or piezoelectric valve 760,960 is required to facilitate depressurization and pressurization of thegas within the PSA case 950, and to output the oxygen enriched gas 216from the PSA system 700, 900 to the user. By using piezoelectricmicroblowers 816, the PSA system 900 can transition each individualmicroblower 816 or microblower array 810 between ON or OFF statesextremely rapidly using MOSFET switches 812. For example, a pulse widthmodulation control can simulate a 26 kHz square wave form of thepiezoelectric microblowers 816, precisely controlling the piezoelectricoscillations in order to power the microblowers ON or OFF without anypartial oscillations, and as such, producing full depressurization andpressurization cycles even at extremely rapid PSA cycle times.

Further, the opposing set or array 810 of piezoelectric microblowers 816can be placed on a printed circuit board (PCB) 910 to facilitate thecyclical pressurization and depressurization. With an opposed set ofpiezoelectric microblowers, it is possible to construct an ultra-rapidvacuum pressure swing adsorption system 10 while reducing the number ofvalves required, improving separative performance based on theadsorption isotherm.

IX. Oxygen Concentrator Functioning as CPAP or BIPAP Device

In one embodiment, a PSA system 10, such as the PSA system 300 shown inFIG. 3A, can be configured such that a user patient using the PSA system300 may exhale through an exhalation outlet (not shown) that mayfunction separately or in conjunction with the valve 340, for example ina wye-type configuration, such that carbon dioxide (CO2) rich gasoutputted from the user during the user's exhalation phase is notre-inhaled by the user with enriched oxygen gas 216 produced during anadsorption phase 211 for the PSA cycle and outputted to the user duringthe user's inhalation phase. In some instances, such as for those userswith obstructive sleep apnea, it may be advantageous to provideabove-atmospheric pressure during the exhalation phase, also known inprior art as positive end expiratory pressure (PEEP). In one embodiment,this positive pressure could be provided by the compressor 310 as shownin FIG. 3A, where valve 340 can be configured as a 3-way valve or aseparate valve (not shown) can be added to the PSA system 300, such thatcompressed air 236 can be routed via the valve 360 configured as a 3-wayvalve, to the user during the desorption phase 241 of the PSA cycle.During the desorption phase 241 of a PSA cycle, oxygen enriched gas 216from the oxygen purge tank 330 flows through the adsorption column 320such that nitrogen is removed (desorbed) from the adsorption column 320and flushed as gaseous nitrogen to the atmosphere via the nitrogenrelease valve 370. During the PSA cycle desorption phase 241, valve 340is closed and valve 370 is open, such that no output gas is delivered tothe user during the desorption phase 241. In this embodiment, where thePSA cycle is modified to provide above-atmospheric pressure to the userduring the user's exhalation phase, the compressor 310 would be operatedcontinuously or in a manner such that positive end expiratory pressurecould be provided to the user. In this instance, the 3-way valve 360would be opened such that the compressed air 236 generated by thecontinuously operating compressor 310 is routed to the user output gasoutlet after the closed valve 340, and valve 360 would be selectivelyclosed such that the compressed air 236 could not flow through the valve360 to the adsorption column 320. In this configuration, the desorptionof the adsorption column 320 continues in a closed circuit comprisingthe oxygen purge tank 330, the valve 330 and 370, and the adsorptioncolumn 320, while concurrently the pressurized air 236 produced by thecompressor is routed through valve 360 to the user output gas outlet toprovide pressurized air 236 to the user during the user's exhalationphase, as illustrated by the phase graph 20E shown in FIG. 1I.

Further, in one embodiment, the motor speed of the blower or compressor310 can be adjusted by the controller 380, using one or more algorithmsand/or feedback control such that the pressure and flowratecharacteristics of the pressurized air 236 outputted by the compressor310 to provide PEEP to the user can be altered using data from breathingcycle sensors 16, 18, including, for example, pressure sensors or massair flowrate sensors. In one embodiment, a compressor 310 with >30 cmH2Opressure, similar to prior art oxygen concentrators, could be utilizedfor the PSA oxygen generating process, wherein air could be accumulatedin an air pressure tank 332 (see FIG. 3H) during the desorption phase241, and a separate blower (not shown) could be utilized to provide PEEPbetween 0.1-30 cmH2O pressure to the user during the user's exhalationphase, allowing an oxygen concentrator including a pulsed PSA system 10to function as a continuous positive airway pressure (CPAP) device or asa bilevel positive airway pressure (BiPAP) device.

In another example configuration is shown FIGS. 13A-13B, a PSA system850 operable to function as a CPAP device or as a BiPAP device isillustrated. FIG. 13A illustrates the valve configuration 851 of the PSAsystem 850 during an adsorption phase 211, where enriched oxygen gas 216is outputted to the user via valve 858. FIG. 13B illustrates the valveconfiguration 853 of the PSA system 850 during a desorption phase 241,where pressurized air 236 is outputted to the user via a pressureregulator while concurrently, desorption of the adsorption column 320 isconducted.

Referring to FIG. 13A, during the adsorption phase 211, a first positionof valve 360 is closed, and a second position of valve 360 is open, suchthat compressed air 236 flows from the compressor/blower 858 to theadsorption column 320, where nitrogen is adsorbed from the air andoxygen enriched gas 216 is output via open valve 350, the oxygen purgetank 330 and open valve 856 to a user, in sync with the inhalation phaseof the user's breathing cycle 202. Valve 852 is closed during theadsorption phase 211.

During the oxygen purge phase 221 following the adsorption phase 211,the first position of valve 360 is closed, and the second position ofvalve 360 is open to flow compressed air 236 through the adsorptioncolumn 320. Valve 852 is closed. Valve 350 is open and valve 856 isclosed, such that enriched oxygen gas 216 accumulates in the O2 purgetank 330, however is not outputted to the user. The first position ofvalve 360 is opened, such that pressurized air 236 flows to user fromthe compressor 858. In one example a pressure regulator 854 can beincluded in the PSA system 850, as shown in FIG. 13A, to regulate thepressure level of the compressed air 236 being outputted from the blower858 to the user as PEEP. In one example, the controller 380 (not shown)can be configured to actuate the oxygen purge phase 211 at the beginningof the dead space period of the user's inhalation phase. In anotherexample shown in FIG. 15, the oxygen purge phase 221 can be eliminatedfrom the PSA cycle by the use of a vacuum desorption process, such thatthe PSA cycle transitions directly to the desorption phase 241 from theadsorption phase 211.

During the desorption phase 241, as shown in FIG. 13B, the firstposition of valve 360 is open such that pressurized air 236 outputtedfrom the compressor/blower 858 flows to the user, via a pressureregulator 854 in the example shown, as PEEP. The desorption phase 241 issynchronized with the user's breath flow phases such that the desorptionphase 241 and the flow of PEEP to the user is initiated during anon-productive portion of the user's breathing cycle 202, for example,as shown in FIG. 1I, during the dead space period of the inhalationphase, or during the exhalation phase. Concurrently with flowingpressurized air 236 as PEEP to the user, the desorption phase 241 of thePSA cycle is actuated, where during the desorption phase 241, the secondposition of valve 360 is closed to prevent compressed air 236 fromflowing to the adsorption column 320 from the compressor/blower Position1 for Valve 260 open, Position 2 for Valve 260 closed. Valve 240 closed.Valve 250 and Valve 270 open. Enriched O2 from O2 purge tank 230 flowsback through adsorption column 220. N2 flows out through Valve 270 toatmosphere.

Referring to FIG. 13C, shown is another example configuration of apulsed PSA (PPSA) system 860 which can be controlled to outputpressurized air 236 to a user during the desorption phase 241 of the PSAcycle. In the example shown in FIG. 13C, during the adsorption phase211, position A for valve 260 is closed and position B for valve 260 isopen, such that compressed air 236 flows from the compressor 210 throughthe adsorption column 220. During the adsorption phase 211, valve 270closed, valves 250 and 240 are open, such that the enriched oxygen gas261 generated in the adsorption column 220 by absorption of nitrogenfrom the incoming air 236 is outputted to the user. In one example, thePSA system 860 includes a controller 380 which synchronizes actuation ofthe adsorption phase 211 with a production portion of the user's breathflow phases, such that, for example, the adsorption phase 211 isinitiated at the beginning of a pre-inhalation period of the user'sexhalation phase or at the beginning of a user inhalation phase.

An O2 purge phase 221 of the PSA cycle is actuated, for example, at thebeginning of a dead space period of the user's inhalation phase, whereduring the O2 purge phase 221, position A for valve 260 is closed andposition B for valve 260 is opened such that compressed air flows fromthe compressor 210 through the adsorption column 220. Valves 240 and 270are closed and valve 250 is open during the O2 purge phase 221, suchthat enriched oxygen gas 216 accumulates in the O2 purge tank 230,however no enriched oxygen gas 216 is provided to user. Rather,pressurized air 236 flows to the user from the compressor 210. In oneexample, the pressure of the pressurized air 236 flowing to the user isregulated by a pressure regulator 854, according to the user'srequirements. The O2 purge phase 221 can be eliminated from the PSAcycle, as previously described herein, with the use of vacuum assisteddesorption.

A desorption phase 241 of the PSA cycle is actuated, for example, at thebeginning of the user's exhalation phase, where during the desorptionphase 241, position A for valve 260 is open and position B for valve 260closed, valve 240 is closed, and valves 250 and 270 are open. During thedesorption phase 241, enriched oxygen gas 216 from the O2 purge tank 230flows back through adsorption column 220 and nitrogen is desorbed in theform of nitrogen gas, which is vented from the PSA system 10 throughvalve 270 to the atmosphere.

In another example configuration illustrated by FIG. 14, a pulsed PSA(PPSA) system 870 including a compressor 210 and a separate blower 872is shown. In this example, the separate blower is actuated to providepressurized air 236 to the user during time periods when enriched oxygengas 216 is not being outputted to the user from the PSA system 870. Inan illustrative example, the blower 872 continuously providespressurized air 236 to the user during the user exhalation phase, andduring the O2 purge 221 and desorption 241 phases performed by the PSAsystem 870. This configuration permits dedicated use of the compressor210 to support on-demand production of enriched oxygen gas 216synchronized to the user's breath flow phases, and/or to allowaccumulation of compressed air 236 in an air volume tank (not shown)which allows higher flowrates of enriched oxygen gas 216 to be providedto the user during the inhalation phases of user breathing. The blower872, in the example shown, outputs a lower pressure air flow 236 whichcan be provided to the user as PEEP during the user exhalation phases.

In the example shown in FIG. 14, the adsorption phase 211 is actuated byopening valve 260 and closing valve 270, and powering on the compressor210 to flow compressed air through the adsorption column 220. Theadsorption phase 211 is synchronized with the user's breathing patternsuch that the enriched oxygen gas 216 outputted from the adsorptioncolumn 220 flows through open valve 240 to the user during theproduction portion of the user's breathing cycle, as previouslydescribed herein.

In a next step, the blower 872 is actuated concurrent with initiation ofthe O2 purge phase 221 of the PSA cycle, which could occur, for example,during the anatomical dead space period of the user's inhalation phaseor any other phase of the user breathing cycle. During the O2 purgephase 221, the compressor 210 is powered on and flows compressed air 236through the adsorption column 220. During the O2 purge phase, valve 260is open and valve 270 and 240 are closed, such that enriched oxygen gas216 from the adsorption column 220 accumulates in the O2 purge tank 230,while pressurized air from the blower 872 flows to user continuously,such that performance of the PSA cycle and generation of PEEP to theuser occur independently of each other in this example embodiment.

In a next step, the desorption phase 241 of the PSA cycle is initiated.During the desorption phase 241, which is synchronized with the user'sexhalation phase, the blower 872 continues to independently andcontinuously output pressurized air 236 to the user during the user'sexhalation phase and for the duration of the desorption phase 241.During the desorption phase 241, the compressor 210 can either bepowered off to provide an energy savings to the PSA system 870, or airvolume tank can be added to the PSA system 870 such that pressurized airoutputted from the compressor 210 during the desorption phase can beaccumulated for use during a subsequent adsorption phase 211. In thisexample, with the compressor 210 continuously powered on, valve 260 isclosed to prevent the flow of compressor air to the adsorption column220, allowing desorption of the adsorption column 220 to occur whileaccumulating pressurized air from the compressor 210 in an air volumetank. Valve 270 is open and valve 240 is closed such that oxygenenriched gas flows from the O2 purge tank 230 back through adsorptioncolumn 220 and nitrogen is desorbed from the adsorption bed as nitrogengas, which flows out through valve 270 to the atmosphere.

In another example configuration of a pulsed PSA (PPSA) system 880 shownin FIG. 15, the PPSA system 880 includes a combination compressor andvacuum pump 882, such that an O2 purge tank is not required, and the PSAcycle is performed without an O2 purge phase 221. In one embodiment, thecombination compressor and vacuum pump 882 could be enabled either usinga dual-head compressor or having separate pressure and vacuum pumps.During the absorption phase 221, the valve 260 is open for position Band valve 270 is closed. Pressurized air 236 flows through theadsorption column 220 to generate enriched oxygen gas 216 which isflowed to user via the open valve 240. Valve 260 in position A isclosed, and the vacuum pump portion of pump 882 is powered off.

During the vacuum assisted desorption phase 241, valve 260 is closed forposition B and open for position A. Valve 270 is open and valve 240 isclosed. Both the compressor and vacuum of pump 882 are powered on, suchthat nitrogen is desorbed from the adsorption column 220 using vacuumpressurized air from the vacuum portion of pump 882, while concurrently,the compressor function of pump 882 outputs pressurized air 236 to theuser via position A of valve 260.

The example shown in FIG. 15 is non-limiting, and variations of thisconfiguration could be used. For example, a two-way valve can besubstituted for the three-way valve 260, and a separate blower can beadded to deliver pressurized air 236 to the user during the exhalationphase.

X. Additional Configurations

The illustrative configurations of the PSA system 10 described hereinare non-limiting examples of PSA system 10, such that otherconfigurations of the PSA system 10 can be included within the scope ofthe description. For example, an ultra-rapid pressure swing adsorption(URPSA) system using piezoelectric microblowers 816 regulated by MOSFET812 can be reduced in size even further through the incorporation ofmicrofabrication and microelectromechanical system (MEMS) componentsinto the PSA system 10. As used herein, the term “MEMS” refers tocomponents and/or devices that range in size from 1 micron to 1000microns (1 mm). By way of illustrative example, MEMS components and/ordevices which can be incorporated into the PSA system 10 to shrink thepackaging size of the oxygen concentrator including the PSA system 10can include microfabricated wafer thin zeolite adsorbents, micro-scaleMEMS air blowers, and ultra-fast actuating MEMS microvalves. In anotherexample, NEMS devices can be utilized to create microchip and transistorscale pressure swing adsorption systems and can be fabricated usingsemiconductor manufacturing techniques found in optoelectronics andphotolithography. As used herein, the term “NEMS” refers to componentsand/or devices that are less than 1 micron in size.

In one example of the invention described above, a microphone andamplifier can be incorporated into the PSA system 10 and/or into theoxygen delivery device 342, instead of or in addition to the pressuresensor 16 of the PSA system 10. In this configuration, a respirationsensing microphone and/or an amplifier detect sound from a user when theuser begins respiration, e.g., begins an inhalation phase. Thecontroller 380 receives an amplified signal from the microphoneindicating the onset of the user's inhalation phase, and activates theadsorption phase 211 of the PSA cycle. The dosage of the enriched oxygengas 216 provided to the user, in this example, could be in proportion tothe signal strength of the respiration sensor. Like that of the pressuresensor, the controller 380 of the PSA system 10 can also configuresettings such that a threshold signal must be detected for theadsorption and/or desorption phases 211, 241 to begin and/or end. Thelocation of the microphone and amplifier in this example can benon-invasive to the user, located at the portion of the PSA system 10where the user physically engages the PSA system, via a nasal cannula 12for example.

In one example of the pulsed pressure swing adsorption (PPSA) system, amulti-bed pressure swing adsorption system 10 can also be utilized,where the adsorption phase 211 of each adsorption bed of the multi-bedsystem is synchronized with different flow phases of the user's breath,and/or with different periods within the flow phases of the user'sbreath. For example, asynchronous cycle times can be achieved utilizingthe two adsorbent beds with a similar control system described inprevious configurations herein.

In one example of an ultra-rapid pressure swing adsorption (URPSA)system, a macro scale variant can be created such that low pressurechange, high volumetric flow blowers, ultra-rapid cycle times, and lowlength to diameter (L:D) ratio adsorbent materials are utilized.Further, the flow blowers do not need to be microblowers 816. Instead,the flow blowers can include larger macroscale fan blowers orcentrifugal pumps. Other air compressor types or blowers can also beutilized including but not limited to thermoelectric blowers, Teslaturbine type air compressors, bellows air compressors, scroll type aircompressors, wobble type compressors, and reciprocating compressors.

In other embodiments, particularly in ultra-rapid pressure swingadsorption (USPSA) systems 10, passive check valves with low crackingpressures can be utilized instead of actively controlled solenoid valvesor proportional control valves. Further, Tesla valvular conduits couldalso be utilized to simultaneously allow flow in one direction with nocracking pressure constraints and also allow a small percentage ofoxygen to flow backwards during the purge or vacuum desorption phases ofthe PSA cycle.

In one embodiment, the pulsed pressure swing adsorption system couldfunction as a mechanical ventilator wherein a ventilator circuit can beadded to assist a user who cannot spontaneously breathe and may alsorequire supplemental oxygen.

In some embodiments of the invention, the PSA cycle times of the PSAcycles and/or PSA cycle phases may be fixed, which may be advantageousdue to programming simplicity, especially in cases where the cycle timesare rapid or ultra-rapid. Advantageously, this can provide continuousflow output oxygen conservation described herein as being based not onvariable cycle times, but rather based on proportional valve controland/or the sensor control system described herein.

In this specification, reference is made in detail to specificembodiments of the invention. Some of the embodiments or their aspectsare illustrated in the drawings. For clarity in explanation, theinvention has been described with reference to specific embodiments,however it should be understood that the invention is not limited to thedescribed embodiments. The invention covers alternatives, modifications,and equivalents as may be included within its scope as defined by anypatent claims. The preceding embodiments of the invention are set forthwithout any loss of generality to, and without imposing limitations on,the claimed invention. In the preceding description, specific detailsare set forth in order to provide a thorough understanding of thepresent invention. The present invention may be practiced without someor all of these specific details. In addition, well known features maynot have been described in detail to avoid unnecessarily obscuring theinvention.

In addition, it should be understood that steps of the exemplary methodsset forth in this exemplary patent can be performed in different ordersthan the order presented in this specification. Furthermore, some stepsof the exemplary methods may be performed in parallel rather than beingperformed sequentially. The present invention may be practiced withdifferent combinations of the features in each described configuration.

The terminology used herein is for the purpose of describing particularaspects only and is not intended to be limiting of the disclosure. Asused herein, the singular forms “a,” “an,” and “the” are intended tocomprise the plural forms as well, unless the context clearly indicatesotherwise. It will be further understood that the terms “comprises”and/or “comprising,” when used in this specification, specify thepresence of stated features, integers, steps, operations, elements,and/or components, but do not preclude the presence or addition of oneor more other features, integers, steps, operations, elements,components, and/or groups thereof.

While the invention has been particularly shown and described withreference to specific embodiments thereof, it should be understood thatchanges in the form and details of the disclosed embodiments may be madewithout departing from the scope of the invention. Although variousadvantages, aspects, and objects of the present invention have beendiscussed herein with reference to various embodiments, it will beunderstood that the scope of the invention should not be limited byreference to such advantages, aspects, and objects. Rather, the scope ofthe invention should be determined with reference to patent claims.

The invention claimed is:
 1. An oxygen concentrator system comprising: apressure swing adsorption (PSA) system including: a gas outletconfigured to flow oxygen enriched gas to a user of the oxygenconcentrator; the PSA system configured to execute a PSA cycle toproduce the oxygen enriched gas; a sensor in communication with the gasoutlet and the PSA system; wherein the sensor is configured to sense abreathing parameter of a breathing cycle of the user; wherein thebreathing cycle includes a plurality of breaths; wherein the PSA systemis further configured to: receive, from the sensor, a breathing inputdefined by the breathing parameter; determine each respective breath,using the breathing input; and synchronize execution of the PSA cyclewith each respective breath such that a plurality of PSA cycles isexecuted during each respective breath.
 2. The oxygen concentratorsystem of claim 1, wherein each respective breath includes an inhalationphase and an exhalation phase; and wherein the PSA system is configuredto synchronize actuation of the flow of the oxygen enriched gas via thegas outlet with one or more of the inhalation phase and the exhalationphase.
 3. An oxygen concentrator system comprising: a pressure swingadsorption (PSA) system including: a gas outlet configured to flowoxygen enriched gas to a user of the oxygen concentrator; the PSA systemconfigured to execute a PSA cycle to produce the oxygen enriched gas; asensor in communication with the gas outlet and the PSA system; whereinthe sensor is configured to sense a breathing parameter of a breathingcycle of the user; wherein the breathing cycle includes a plurality ofbreaths; wherein the PSA system is further configured to: receive, fromthe sensor, a breathing input defined by the breathing parameter;determine each respective breath, using the breathing input; andsynchronize execution of the PSA cycle with each respective breath suchthat at least one PSA cycle is executed during each respective breath;wherein each respective breath includes an inhalation phase and anexhalation phase; wherein the PSA cycle includes an adsorption phase anda desorption phase; wherein the PSA system is configured to synchronizeexecution of the PSA cycle with the breathing cycle such that: actuationof the adsorption phase is synchronized with the inhalation phase; andactuation of a desorption phase is synchronized with the exhalationphase; wherein the PSA system includes: an adsorption column; an aircompressing device configured to output pressurized air; wherein the gasoutlet, the air compressing device, and the adsorption column are influid communication; wherein the PSA system is configured to selectivelyactuate the air compressing device to perform at least one of theadsorption phase or the desorption phase; wherein the air compressingdevice is a bidirectional device actuable to: in a first direction,output pressurized atmospheric air into the adsorption column during theadsorption phase; and in a second direction, output nitrogen gas fromthe adsorption column during the desorption phase.
 4. The oxygenconcentrator system of claim 3, wherein the bidirectional deviceincludes: a first plurality of microblowers configured to be actuable inthe first direction; and a second plurality of microblowers configuredto be actuable in the second direction.
 5. An oxygen concentrator systemcomprising: a pressure swing adsorption (PSA) system including: a gasoutlet configured to flow oxygen enriched gas to a user of the oxygenconcentrator; the PSA system configured to execute a PSA cycle toproduce the oxygen enriched gas; a sensor in communication with the gasoutlet and the PSA system; wherein the sensor is configured to sense abreathing parameter of a breathing cycle of the user; wherein thebreathing cycle includes a plurality of breaths; wherein the PSA systemis further configured to: receive, from the sensor, a breathing inputdefined by the breathing parameter; determine each respective breath,using the breathing input; synchronize execution of the PSA cycle witheach respective breath such that at least one PSA cycle is executedduring each respective breath; predict, using the breathing input, abreathing waveform of the respective breath; and synchronize an oxygenproduction waveform of the enriched oxygen gas to the breathing waveformfor the respective breath.
 6. An oxygen concentrator system comprising:a pressure swing adsorption (PSA) system including: a gas outletconfigured to flow oxygen enriched gas to a user of the oxygenconcentrator; the PSA system configured to execute a PSA cycle toproduce the oxygen enriched gas; a sensor in communication with the gasoutlet and the PSA system; wherein the sensor is configured to sense abreathing parameter of a breathing cycle of the user; wherein thebreathing cycle includes a plurality of breaths; wherein the PSA systemis further configured to: receive, from the sensor, a breathing inputdefined by the breathing parameter; determine each respective breath,using the breathing input; synchronize execution of the PSA cycle witheach respective breath such that at least one PSA cycle is executedduring each respective breath; wherein each respective breath includesan inhalation phase and an exhalation phase; wherein the PSA system isfurther configured to flow pressurized air via the gas outlet; thesystem further comprising: a controller configured to control flow ofthe oxygen enriched gas and flow of the pressurized air via the gasoutlet; wherein the controller is configured to actuate a flow ofalternating volumes of the oxygen enriched gas and the pressurized airvia the gas outlet during the inhalation phase.